CN212395897U - Automatic liquid level control system for pig gall powder concentration - Google Patents
Automatic liquid level control system for pig gall powder concentration Download PDFInfo
- Publication number
- CN212395897U CN212395897U CN202020946918.6U CN202020946918U CN212395897U CN 212395897 U CN212395897 U CN 212395897U CN 202020946918 U CN202020946918 U CN 202020946918U CN 212395897 U CN212395897 U CN 212395897U
- Authority
- CN
- China
- Prior art keywords
- pipe
- main body
- evaporating pot
- main part
- control system
- 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 - Fee Related
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 26
- 239000000843 powder Substances 0.000 title claims abstract description 19
- 238000001704 evaporation Methods 0.000 claims abstract description 48
- 238000010438 heat treatment Methods 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 238000007789 sealing Methods 0.000 claims description 33
- 230000008020 evaporation Effects 0.000 claims description 21
- 238000001816 cooling Methods 0.000 claims description 13
- 239000002184 metal Substances 0.000 claims description 4
- 230000000694 effects Effects 0.000 abstract description 7
- 238000007599 discharging Methods 0.000 abstract description 4
- 239000006260 foam Substances 0.000 abstract description 4
- 238000009795 derivation Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 3
- 238000005086 pumping Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a liquid level automatic control system for pig gall powder is concentrated, including the evaporating pot main part, evaporating pot main part upper end is equipped with the main part closing cap, and evaporating pot main part outer wall is equipped with the inlet pipe to evaporating pot main part opposite side is equipped with the overflow pipe, the lower extreme of evaporating pot main part is equipped with the discharging pipe, and the inside of evaporating pot main part is equipped with the cooler bin of chamfered frustum shape to the upper end of cooler bin is equipped with a plurality of heating pipe, the upper end of heating pipe is equipped with the circular sheetmetal of cavity form, and the sheetmetal upper end is equipped with the intake pipe, and the intake pipe passes the main part closing cap, overflow pipe one end is equipped with the recess, and the block has the shrouding in the overflow pipe recess to the upper end of shrouding. This evaporating pot with automatic taking out after water is full of water is provided with automatic flowing back structure, can directly discharge water, avoids floating the foam to influence the derivation effect of water. Thereby improving the concentration efficiency of the pig gall powder.
Description
Technical Field
The utility model relates to an evaporating pot technical field specifically is a liquid level automatic control system for pig gall powder is concentrated.
Background
In the production process of the pig gall powder, the pig gall powder needs to be concentrated, and an evaporation tank needs to be used. The steam condensate discharged from the steam drum of the evaporating pot has higher temperature than the steam of the steam drum of the next effect. If the pressure in a container is reduced, self-evaporation is generated, and the vapor in the self-evaporation tank can be used for heating a next-effect evaporation tank or a corresponding heater, and the device is called the self-evaporation tank.
The too much condition of solution can appear at the in-process that uses of current evaporating pot, can appear the condition of froth moreover, and the froth will influence the effect of flowing back, leads to the discharge that can not be timely behind solution reaching the water line. The existing method is that the solution is pumped manually, so that the pumping efficiency is low, and extra personnel are needed.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a liquid level automatic control system for pig gall powder is concentrated to solve the in-process that the evaporating pot was using on the existing market that above-mentioned background art provided, the too much condition of solution can appear, can appear the condition of floating the foam moreover, float the foam and can influence the effect of flowing back, lead to solution can not in time discharge after reaching the water line, and the problem of inefficiency.
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides a liquid level automatic control system for pig gall powder is concentrated, includes the evaporating pot main part, evaporating pot main part upper end is equipped with the main part closing cap, and evaporating pot main part outer wall is equipped with the inlet pipe to evaporating pot main part opposite side is equipped with the overflow pipe, the lower extreme of evaporating pot main part is equipped with the discharging pipe, and the inside of evaporating pot main part is equipped with the cooler bin of chamfered frustum shape to the upper end of cooler bin is equipped with a plurality of heating pipe, the upper end of heating pipe is equipped with the circular sheetmetal of cavity form, and the sheetmetal upper end is equipped with the intake pipe, and the intake pipe passes the main part closing cap, overflow pipe one end is equipped with the recess, and the block has the shrouding in the overflow pipe recess to the upper.
Preferably, the upper end of the main body sealing cover is provided with a cylindrical sealing pipe made of rubber, and the sealing pipe is sleeved on the outer ring of the air inlet pipe.
Preferably, at least 20 heating pipes are arranged, and the heating pipes are uniformly distributed at the upper end of the cooling box.
Preferably, the outer wall of the cooling box is provided with a water outlet pipe, and the water outlet pipe penetrates through the outer wall of the evaporation tank main body.
Preferably, the lower end of the sealing plate is provided with a rectangular fixing plate, and the width of the fixing plate at the lower end of the sealing plate is larger than the width of the inner part of the upper groove of the overflow pipe.
Preferably, the central line of the liquid outlet hole and the central line of the overflow pipe are positioned on the same straight line.
Compared with the prior art, the beneficial effects of the utility model are that: this evaporating pot with automatic taking out after water is full of water is provided with automatic flowing back structure, can directly discharge water, avoids floating the foam to influence the derivation effect of water. The cylindrical seal pipe on the main part closing cap of the device can seal the air inlet pipe all around, plugs up the air inlet pipe gap all around, avoids the condition that the air inlet pipe appears leaking all around, and the fixed plate of shrouding lower extreme can block in the recess below of overflow pipe, avoids the shrouding to break away from in the recess of overflow pipe, and goes out the liquid hole on the shrouding and play the effect of drain, makes the inside solution of evaporating pot main part can enter into in the overflow pipe.
Drawings
FIG. 1 is a schematic structural view of an automatic liquid level control system for pig gall powder concentration according to the present invention;
FIG. 2 is a top view of a heating pipe of the automatic liquid level control system for pig gall powder concentration of the present invention;
fig. 3 is a side view of the liquid level automatic control system sealing plate for pig gall powder concentration of the utility model.
In the figure: 1. the device comprises an air inlet pipe, 2, a main body sealing cover, 3, an evaporation tank main body, 4, an inlet pipe, 5, a heating pipe, 6, a cooling box, 7, a discharging pipe, 8, a floating ball, 9, an overflow pipe, 10, a sealing plate, 11, a water outlet pipe, 12 and a liquid outlet hole.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-3, the present invention provides a technical solution: a liquid level automatic control system for pig gall powder concentration comprises an evaporation tank main body 3, a main body sealing cover 2 is arranged at the upper end of the evaporation tank main body 3, a feeding pipe 4 is arranged on the outer wall of the evaporation tank main body 3, an overflow pipe 9 is arranged on the other side of the evaporation tank main body 3, a cylindrical sealing pipe made of rubber is arranged at the upper end of the main body sealing cover 2, the sealing pipe is sleeved on the outer ring of an air inlet pipe 1, the cylindrical sealing pipe at the upper end of the main body sealing cover 2 of the structure can seal the periphery of the air inlet pipe 1 to avoid the condition of leakage around the air inlet pipe 1, a discharging pipe 7 is arranged at the lower end of the evaporation tank main body 3, a cooling box 6 in a reversed frustum shape is arranged inside the evaporation tank main body 3, a plurality of heating pipes 5 are arranged at the upper end of the cooling box 6, a water outlet pipe 11 is arranged on the outer wall of the cooling box 6, and the water in the cooling box 6 can be discharged through the outlet pipe 11, the upper end of the heating pipe 5 is provided with a hollow round metal sheet, the upper end of the metal sheet is provided with an air inlet pipe 1, the air inlet pipe 1 penetrates through the main body sealing cover 2, at least 20 heating pipes 5 are arranged, the heating pipes 5 are uniformly distributed at the upper end of the cooling box 6, steam can be introduced into the heating pipe 5 of the structure, so that the solution in the evaporating pot main body 3 can be heated through the heating pipe 5, one end of the overflow pipe 9 is provided with a groove, a sealing plate 10 is clamped in the groove of the overflow pipe 9, a floating ball 8 is arranged at the upper end of the sealing plate 10, a liquid outlet hole 12 is arranged on the outer wall of the sealing plate 10, the lower end of the sealing plate 10 is provided with a rectangular fixing plate, the width of the fixing plate at the lower end of the sealing, avoid shrouding 10 to break away from in the overflow pipe 9 upper groove, go out the central line of liquid hole 12 and be in same straight line with the central line of overflow pipe 9, the effect of drain hole 12 of this structure plays the drain, when going out liquid hole 12 and removing overflow pipe 9 position, the inside solution of evaporating pot main part 3 can move to overflow pipe 9 in through going out liquid hole 12.
The working principle is as follows: when the automatic-pumping evaporation tank is used, firstly, the evaporation tank main body 3 of the device is placed at a proper place, then raw materials are guided into the evaporation tank main body 3 through the feeding pipe 4, then steam is guided into the heating pipe 5 through the air inlet pipe 1 on the main body sealing cover 2, the solution in the evaporation tank main body 3 is heated through the heating pipe 5, if the solution in the evaporation tank main body 3 is excessive, the floating ball 8 is jacked up by the solution, the floating ball 8 drives the sealing plate 10 to move upwards, so that the liquid outlet hole 12 on the sealing plate 10 is moved to the position of the overflow pipe 9, the redundant solution in the evaporation tank main body 3 is discharged through the overflow pipe 9, the water in the heating pipe 5 can be discharged through the water outlet pipe 11, and the solution in the evaporation tank main body 3 flows to the position of the discharge pipe 7 through a gap between the outer walls of the cooling tank 6 and is discharged through the discharge pipe 7, thereby completing a series of works.
Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments or portions thereof without departing from the spirit and scope of the invention.
Claims (6)
1. The utility model provides a liquid level automatic control system for pig gall powder is concentrated, includes evaporating pot main part (3), its characterized in that: the upper end of the evaporation tank main body (3) is provided with a main body sealing cover (2), the outer wall of the evaporation tank main body (3) is provided with a feeding pipe (4), an overflow pipe (9) is arranged on the other side of the evaporation tank main body (3), a discharge pipe (7) is arranged at the lower end of the evaporation tank main body (3), and the inside of the evaporating pot main body (3) is provided with a cooling box (6) in a shape of a reversed frustum, a plurality of heating pipes (5) are arranged at the upper end of the cooling box (6), a hollow round metal sheet is arranged at the upper end of each heating pipe (5), an air inlet pipe (1) is arranged at the upper end of each metal sheet, the air inlet pipe (1) penetrates through the main body sealing cover (2), one end of the overflow pipe (9) is provided with a groove, a sealing plate (10) is clamped in the groove of the overflow pipe (9), and the upper end of the sealing plate (10) is provided with a floating ball (8), and the outer wall of the sealing plate (10) is provided with a liquid outlet hole (12).
2. The automatic liquid level control system for pig gall powder concentration according to claim 1, characterized in that: the upper end of the main body sealing cover (2) is provided with a cylindrical sealing pipe made of rubber, and the sealing pipe is sleeved on the outer ring of the air inlet pipe (1).
3. The automatic liquid level control system for pig gall powder concentration according to claim 1, characterized in that: at least 20 heating pipes (5) are arranged, and the heating pipes (5) are uniformly distributed at the upper end of the cooling box (6).
4. The automatic liquid level control system for pig gall powder concentration according to claim 1, characterized in that: the outer wall of the cooling box (6) is provided with a water outlet pipe (11), and the water outlet pipe (11) penetrates through the outer wall of the evaporating pot main body (3).
5. The automatic liquid level control system for pig gall powder concentration according to claim 1, characterized in that: the lower end of the sealing plate (10) is provided with a rectangular fixing plate, and the width of the fixing plate at the lower end of the sealing plate (10) is larger than the width of the inner part of the upper groove of the overflow pipe (9).
6. The automatic liquid level control system for pig gall powder concentration according to claim 1, characterized in that: the central line of the liquid outlet hole (12) and the central line of the overflow pipe (9) are positioned on the same straight line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020946918.6U CN212395897U (en) | 2020-05-29 | 2020-05-29 | Automatic liquid level control system for pig gall powder concentration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020946918.6U CN212395897U (en) | 2020-05-29 | 2020-05-29 | Automatic liquid level control system for pig gall powder concentration |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212395897U true CN212395897U (en) | 2021-01-26 |
Family
ID=74408439
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020946918.6U Expired - Fee Related CN212395897U (en) | 2020-05-29 | 2020-05-29 | Automatic liquid level control system for pig gall powder concentration |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212395897U (en) |
-
2020
- 2020-05-29 CN CN202020946918.6U patent/CN212395897U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN212395897U (en) | Automatic liquid level control system for pig gall powder concentration | |
| CN109925748A (en) | It is a kind of that the liquid degassing device and method of removing gas liquid can be automatically continuously provided | |
| CN102230292B (en) | Circulation cooling device for chute of soda recovery furnace | |
| CN204752245U (en) | Exhaust type is sour, alkali batch meter | |
| CN206235235U (en) | A kind of coil heat exchanger cleaning device | |
| CN211199180U (en) | Fermented grain material distillation equipment for production of unstrained wine | |
| CN210886251U (en) | High-temperature electrolysis condensate water recovery system | |
| CN203479046U (en) | Device for recycling condensate steam in process of production | |
| CN210711479U (en) | Full-automatic wine brewing equipment | |
| CN207256649U (en) | Minute-pressure water injection vacuum system | |
| CN218357505U (en) | Capillary evaporation dehydrator | |
| CN202425565U (en) | Degasser using steam for evacuation and as heating medium | |
| CN210267175U (en) | High-temperature steam generator | |
| CN207619057U (en) | A kind of environmental protection deaerating plant | |
| CN209355218U (en) | A kind of energy-saving pipe frame of boiler | |
| CN210278724U (en) | Special methacrylic acid ester type liquid ring vacuum pump absorption liquid circulating device | |
| CN205191543U (en) | Thermal deoxidizing device | |
| CN215566944U (en) | Cooling type vacuum device | |
| CN219213805U (en) | Sealed vulcanizing tank | |
| CN215335745U (en) | Automatic condensed water treater for condensed water generated by cold heat of pipeline | |
| CN211587850U (en) | Device for preventing dead water pollution in drainage of biological pharmaceutical process pipeline | |
| CN215918051U (en) | Automatic circulation device for dumbbell plastic dipping liquid | |
| CN214620696U (en) | Efficient energy-saving heat exchange unit | |
| CN209371209U (en) | Unattended type pure steam generator | |
| CN214436706U (en) | Integrated small-sized electric heating type swill oil separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220721 Address after: 351100 No. 139, Xincuo, Zhangpu village, Laidian Town, Xianyou County, Putian City, Fujian Province Patentee after: NANFENG BIOCHEMICAL CO.,LTD. Address before: 351254 No.333 Haiping South Road, Fengting Town, Xianyou County, Putian City, Fujian Province Patentee before: Fujian nangu Biotechnology Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20210126 |