CN201848236U - Hydrolyzing tower - Google Patents
Hydrolyzing tower Download PDFInfo
- Publication number
- CN201848236U CN201848236U CN2010202236514U CN201020223651U CN201848236U CN 201848236 U CN201848236 U CN 201848236U CN 2010202236514 U CN2010202236514 U CN 2010202236514U CN 201020223651 U CN201020223651 U CN 201020223651U CN 201848236 U CN201848236 U CN 201848236U
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Abstract
The utility model relates to a hydrolyzing tower, which mainly comprises a tower body, an emptying port, a safety valve port, a pressure gauge port, a discharging port, a water inlet, steam inlets, a heat-conducting oil return port, a heat-conducting oil inlet, a manhole, a feeding port, a pollutant discharging port, water-dividing plates and a heat-conducting oil coil pipe, and is characterized in that the emptying port, the safety valve port and the pressure gauge port are installed at the top of the tower body, the discharging port is installed at one side at the upper part of the tower body, the water inlet is installed at the other side at the upper part of the tower body, the steam inlets are respectively installed at the middle upper part and the middle part of the tower body, the heat-conducting oil return port and the heat-conducting oil inlet are installed at the middle lower part of the tower body, the manhole is installed at one side at the lower part of the tower body, the feeding port is installed at the other side at the lower part of the tower body, the pollutant discharging port is installed at the bottom of the tower body, a plurality of water-dividing plates are installed inside the tower body, and the heat-conducting oil coil pipe is installed at the lower part inside the tower body. In the utility model, the temperature-rise speed can be increased, the pressure steadiness is kept, the hydrolyzing time is shortened, oil and water are uniformly mixed, the hydrolysis ratio is increased, and the purposes of saving the energy and reducing the consumption are achieved.
Description
Technical field
The utility model relates to oil fatty acid hydrolysis device field, is specially a kind of hydrolysis tower.
Background technology
At present, hydrolysis process is ordinary-pressure hydrolysis and the hydrolysis of Dan Ta gap, and ordinary-pressure hydrolysis does not use substantially, and hydrolysis pressure in Dan Ta gap is 0.8Mpa, does not have the water of branch plate, hydrolysis time 10～12 hours, and hydrolysis time is long, and hydrolysis is incomplete, the hydrolysis rate variance; And the steam rate of warming is slow, the high ebb stage occurs through regular meeting, causes steam pressure just to fluctuate, and influences hydrolysis effect, and reduces vapour pressure suddenly, more can cause the interior material of tower to enter in the jet chimney, causes producing instability, poor product quality.
The utility model content
The technical problem that the utility model solved is to provide a kind of hydrolysis tower, to solve the shortcoming in the above-mentioned background technology.
The technical problem that the utility model solved realizes by the following technical solutions:
A kind of hydrolysis tower mainly comprises tower body, evacuation port, relief valve port, gauge port, discharging opening, water inlet, steam inlet, conduction oil is answered back, heat conductive oil inlet, manhole, charging aperture, sewage draining exit divides the water plate, conduction oil coil pipe etc., evacuation port is equipped with at the top of described tower body, relief valve port and gauge port, and a side on tower body top is equipped with discharging opening, the opposite side on tower body top is equipped with water inlet, steam inlet is equipped with at the middle and upper part of tower body and middle part respectively, and the tower body middle and lower part is equipped with that conduction oil is answered back and heat conductive oil inlet, and a side of tower body bottom is equipped with manhole, the opposite side of tower body bottom is equipped with charging aperture, sewage draining exit is equipped with in the bottom of tower body, and several minutes water plate is equipped with in the inside of tower body, and the conduction oil coil pipe is equipped with in the below of the inside of tower body.During operation, material is entered in the tower by charging aperture, the control time of staying of material in tower is 8 hours, and water enters in the tower from water inlet, simultaneously in the conduction oil control tower hydrolysis temperature at 200～210 ℃, pressure 1.8Mpa, divide water plate substep through multilayer, profit evenly exchanges, and falls at the bottom of the tower, promptly finishes hydrolysis.
In the utility model, the inner and upper of described charging aperture is equipped with one group of conduction oil coil pipe, can control the size and the aperture of heat conduction valve according to column bottom temperature.
In the utility model, the water plate was three to four layers in described minute, and evenly was drilled with aperture on the branch water plate.
Beneficial effect:
The utility model can be accelerated programming rate, keep-ups pressure steadily, shortens hydrolysis time, evenly mixes profit, has improved percent hydrolysis, has reached energy saving purposes.
Description of drawings
Fig. 1 is a schematic diagram of the present utility model
The specific embodiment
For technological means, creation characteristic that the utility model is realized, reach purpose and effect is easy to understand, below in conjunction with concrete diagram, further set forth the utility model.
Referring to a kind of hydrolysis tower schematic diagram of Fig. 1, comprise tower body 1, evacuation port 2, relief valve port 3, gauge port 4, discharging opening 5, water inlet 6, steam inlet 7, conduction oil answer back 8, heat conductive oil inlet 9, manhole 10, charging aperture 11, sewage draining exit 12, divide water plate 13, conduction oil coil pipe 14, present embodiment are the embodiment of a hydrolysis tower.
Evacuation port 2 is equipped with at the top of tower body 1, relief valve port 3 and gauge port 4, one side on tower body 1 top is equipped with discharging opening 5, the opposite side on tower body 1 top is equipped with water inlet 6, steam inlet 7 is equipped with at the middle and upper part of tower body 1 and middle part respectively, tower body 1 middle and lower part is equipped with conduction oil and is answered back 8 and heat conductive oil inlet 9, one side of tower body 1 bottom is equipped with manhole 10, the opposite side of tower body 1 bottom is equipped with charging aperture 11, sewage draining exit 12 is equipped with in the bottom of tower body 1, several minutes water plate 13 is equipped with in the inside of tower body 1, and conduction oil coil pipe 14 is equipped with in the below of the inside of tower body 1.
In the present embodiment, the inner and upper of charging aperture 11 is equipped with one group of conduction oil coil pipe 14, can control the size and the aperture of heat conduction valve according to column bottom temperature; Dividing water plate 13 is three to four layers, and evenly is drilled with aperture on the branch water plate 13.During operation, material is entered in the tower by charging aperture 11, the control time of staying of material in tower is 8 hours, and water enters in the tower from water inlet 6, simultaneously in the conduction oil control tower hydrolysis temperature at 200～210 ℃, pressure 1.8Mpa, divide the water plate 13 substeps through multilayer, profit evenly exchanges, and falls at the bottom of the tower, promptly finishes hydrolysis.
More than show and described basic principle of the present utility model and principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; that describes in the foregoing description and the specification just illustrates principle of the present utility model; under the prerequisite that does not break away from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall in claimed the utility model scope.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (3)
1. a hydrolysis tower mainly comprises tower body, evacuation port, relief valve port, gauge port, discharging opening, water inlet, steam inlet, conduction oil is answered back, heat conductive oil inlet, manhole, charging aperture, sewage draining exit, divide the water plate, the conduction oil coil pipe is characterized in that, evacuation port is equipped with at the top of described tower body, relief valve port and gauge port, one side on tower body top is equipped with discharging opening, and the opposite side on tower body top is equipped with water inlet, and steam inlet is equipped with at the middle and upper part of tower body and middle part respectively, the tower body middle and lower part is equipped with that conduction oil is answered back and heat conductive oil inlet, one side of tower body bottom is equipped with manhole, and the opposite side of tower body bottom is equipped with charging aperture, and sewage draining exit is equipped with in the bottom of tower body, several minutes water plate is equipped with in the inside of tower body, and the conduction oil coil pipe is equipped with in the below of the inside of tower body.
2. a kind of hydrolysis tower according to claim 1 is characterized in that, the inner and upper of described charging aperture is equipped with one group of conduction oil coil pipe.
3. a kind of hydrolysis tower according to claim 1 is characterized in that, the water plate was three to four layers in described minute, and evenly is drilled with aperture on the branch water plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202236514U CN201848236U (en) | 2010-06-11 | 2010-06-11 | Hydrolyzing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202236514U CN201848236U (en) | 2010-06-11 | 2010-06-11 | Hydrolyzing tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201848236U true CN201848236U (en) | 2011-06-01 |
Family
ID=44090651
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202236514U Expired - Lifetime CN201848236U (en) | 2010-06-11 | 2010-06-11 | Hydrolyzing tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201848236U (en) |
-
2010
- 2010-06-11 CN CN2010202236514U patent/CN201848236U/en not_active Expired - Lifetime
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Jiangxi Longchang Bio Energy Technology Co., Ltd. Assignor: JIUJIANG LISHAN ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. Contract record no.: 2015360000128 Denomination of utility model: Hydrolyzing tower Granted publication date: 20110601 License type: Exclusive License Record date: 20150811 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110601 |
|
| CX01 | Expiry of patent term |