CN207085368U - A kind of steam flash of APG and alcohol ether glucoside processing fills body device - Google Patents
A kind of steam flash of APG and alcohol ether glucoside processing fills body device Download PDFInfo
- Publication number
- CN207085368U CN207085368U CN201720833877.8U CN201720833877U CN207085368U CN 207085368 U CN207085368 U CN 207085368U CN 201720833877 U CN201720833877 U CN 201720833877U CN 207085368 U CN207085368 U CN 207085368U
- Authority
- CN
- China
- Prior art keywords
- tank body
- steam
- outlet
- heat pump
- apg
- 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
- -1 alcohol ether glucoside Chemical class 0.000 title claims abstract description 19
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 title claims abstract description 19
- 229930182478 glucoside Natural products 0.000 title claims abstract description 19
- 230000008676 import Effects 0.000 claims abstract description 19
- 125000006850 spacer group Chemical group 0.000 claims abstract description 15
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 238000007689 inspection Methods 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000004519 manufacturing process Methods 0.000 abstract description 11
- 238000010438 heat treatment Methods 0.000 description 8
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Landscapes
- Investigating Or Analyzing Materials Using Thermal Means (AREA)
Abstract
The steam flash of a kind of APG and alcohol ether glucoside processing fills body device, be by：Tank body, upper spacer, lower clapboard, it is upper inspection population, liquid level gauge mouth, heat pump outlet, temperature-measuring port, pressure tap, steam outlet, upper standby mouth, under standby mouth, safe valve inlet, steam condensate import, heat pump import, steam condensate outlet, side inspection chamber composition；Tank body both ends are respectively arranged below horizontal bearing, waterline is provided with tank body, the top of tank body one end waterline sets upper spacer, lower clapboard is set between tank body other end waterline and upper spacer, water sets slope under lower clapboard, and steam condensate outlet is reserved in lower clapboard slope bottom；The utility model uses steam flash equipment in APG production process, and the consumption of vapor is greatly reduced, and reduces APG and alcohol ether glucoside production cost, rationally using vapor, energy-conserving and environment-protective, reduces the pollution to environment.
Description
Technical field
The utility model is related to processing APG and alcohol ether glucoside steam flash system, especially a kind of APG and
The steam flash of alcohol ether glucoside processing fills body device.
Background technology
At present, APG and the main production cost of alcohol ether glucoside have feedstock fat alcohol, glucose and hydrogen peroxide, heat energy
Consumption, power consumption, as market competition is growing more intense；The production of APG and alcohol ether glucoside, the mode of heating of use have
Heat-conducting oil heating and vapor heating, heat-conducting oil heating investment is big, also consumes the huge energy, causes cost height, heat
Utilization rate is not high；In view of the foregoing, it is proposed that a kind of steam flash of APG and alcohol ether glucoside processing fills body device.
Utility model content
The purpose of this utility model is to overcome the production of existing APG and alcohol ether glucoside, main production cost
There are feedstock fat alcohol, glucose and hydrogen peroxide, thermal energy consumption, power consumption, as market competition is growing more intense；APG and
The production of alcohol ether glucoside, the mode of heating of use have heat-conducting oil heating and vapor heating, and heat-conducting oil heating investment is big, also consumes
The huge energy, causes cost height, and heat utilization ratio is not high；By reasonably designing, there is provided a kind of APG and alcohol
The steam flash of ether glucosides processing fills body device, and the utility model uses steam flash equipment in APG production process, greatly
Width reduces the consumption of vapor, reduces APG and alcohol ether glucoside production cost, rationally utilizes vapor, energy-saving ring
Protect, reduce the pollution to environment.
The utility model to achieve these goals, adopts the following technical scheme that：A kind of APG and alcohol ether glucoside add
The steam flash of work fills body device, be by：Tank body, upper spacer, lower clapboard, upper inspection population, liquid level gauge mouth, heat pump outlet, survey
Warm mouth, pressure tap, steam outlet, upper standby mouth, under standby mouth, safe valve inlet, steam condensate import, heat pump import,
Steam condensate outlet, side inspection chamber are formed；Tank body both ends are respectively arranged below horizontal bearing, and water level is provided with tank body
Line, the top of tank body one end waterline set upper spacer, lower clapboard are set between tank body other end waterline and upper spacer, under every
Water sets slope under plate, and steam condensate outlet is reserved in lower clapboard slope bottom；
Above the end of tank body one end, two liquid level gauge mouths are respectively arranged below, tank body side sets side inspection chamber；
Tank base side is set up in parallel two heat pump imports, standby mouth under heat pump inlet side is set, and tank base is another
Side sets steam condensate outlet；
Tank body top center sets heat pump to export, heat pump outlet side set gradually respectively one it is upper check population, one
Steam outlet, two pressure taps, a temperature-measuring port；Heat pump outlet opposite side set gradually respectively a standby mouth, one
Safe valve inlet, a steam condensate import.
Beneficial effect：The utility model uses steam flash equipment in APG production process, and water steaming is greatly reduced
The consumption of gas, APG and alcohol ether glucoside production cost are reduced, rationally using vapor, energy-conserving and environment-protective, is reduced to environment
Pollution.
1. steam condensate import enters from one end of flashing apparatus, fall in the solid separator of upper strata, slowly flow to down certainly
On dividing plate, upper spacer and the liquid level in flashing apparatus.Flow velocity is small on upper spacer, and the water that can accelerate steam condensate steams
Gas is evaporated, and the vapor flashed off is entered in Low pressure steam pipeline from steam outlet mouth, steam condensate import and water
Vapor outlet port can not be within close proximity.
2. lower clapboard is 2 ° with the liquid level angle in flashing apparatus, condensate liquid is set to flow to the other end of flashing apparatus,
A diameter of 400mm hole is opened in other end, steam condensate is fallen into the bottom of flashing apparatus, the vapor flashed off is from water
Vapor outlet port mouth is entered in Low pressure steam pipeline.
3. the steam that flashing apparatus bottom flashes off enters the top of flashing apparatus from a diameter of 400mm of lower clapboard hole
Portion, the vapor flashed off are entered in Low pressure steam pipeline from steam outlet mouth.
4. flashing apparatus bottom sets steam condensate outlet, liquid level is discharged higher than 52% from steam condensate outlet；Inspection
When repairing, it is necessary to from steam condensate outlet emptying.
5. flashing apparatus bottom sets heat pump import, heat pump cycle to the heat pump outlet of flashing apparatus top, heat pump outlet exists
120 ° of spiral nozzle is set in flashing apparatus, steam flash is reached maximization.Heat pump outlet is located at flashing apparatus pars intermedia
Position, do not influence to flash the gas flow of vapor, while do not influence installation and maintenance of the spiral nozzle inside flashing apparatus.
6. setting safe valve inlet at the top of flashing apparatus, ensure flashing apparatus safety.
7. setting the standby mouth of gas and the standby mouth of liquid at the top and bottom of flashing apparatus respectively, changed temporarily for pipeline.
8. at the top of flashing apparatus and side sets inspection manhole respectively, dividing plate upper strata can be overhauled and safeguarded, while can be with
Repair below dividing plate.
9. one end of flashing apparatus lower clapboard sets liquid level gauge mouth, for measuring the liquid level of flashing apparatus.
Brief description of the drawings
The utility model is described in further detail below in conjunction with the accompanying drawings：
Fig. 1 is general assembly structural representation；
Fig. 2 is the lower clapboard structural representation in Fig. 1；
Fig. 3 is the upper spacer structural representation in Fig. 1；
Fig. 4 is the cross section structure schematic diagram in Fig. 1；
In Fig. 1,2,3,4：Tank body 1, upper spacer 2, lower clapboard 3, upper inspection population 4, liquid level gauge mouth 5, heat pump outlet 6, survey
Warm mouth 7, pressure tap 8, steam outlet 9, upper standby mouth 10, under standby mouth 11, safe valve inlet 12, steam condensate import
13rd, heat pump import 14, steam condensate outlet 15, side inspection chamber 16.
Embodiment
The utility model is described in further detail with embodiment below in conjunction with the accompanying drawings：
The both ends of tank body 1 are respectively arranged below horizontal bearing, are provided with waterline in tank body 1, one end waterline of tank body 1 it is upper
Portion sets upper spacer 2, and lower clapboard 3 is set between the other end waterline of tank body 1 and upper spacer 2, and 3 times water of lower clapboard set slope,
Reserve steam condensate outlet 15 in the slope bottom of lower clapboard 3；
Above the end of the one end of tank body 1, two liquid level gauge mouths 5 are respectively arranged below, the side of tank body 1 sets side scrutineer
Hole 16；
The bottom side of tank body 1 is set up in parallel two heat pump imports 14, standby mouth 11 under the side of heat pump import 14 is set, tank body
1 bottom opposite side sets steam condensate outlet 15；
The top center of tank body 1 sets heat pump to export 6, heat pump export 6 sides set gradually respectively one it is upper check population 4,
One temperature-measuring port 7 of pressure tap 8, one of steam outlet 9, two；Heat pump export 6 opposite sides set gradually respectively one it is standby
10, safe 12, steam condensate imports 13 of valve inlet of mouth.
Claims (4)
1. a kind of APG and alcohol ether glucoside processing steam flash fill body device, be by：Tank body (1), upper spacer (2), under
Dividing plate (3), upper inspection population (4), liquid level gauge mouth (5), heat pump outlet (6), temperature-measuring port (7), pressure tap (8), steam outlet
(9), upper standby mouth (10), under standby mouth (11), safe valve inlet (12), steam condensate import (13), heat pump import (14),
Steam condensate outlet (15), side inspection chamber (16) are formed；It is characterized in that：Tank body (1) both ends are respectively arranged below water
Flat bearing, is provided with waterline in tank body (1), and the top of tank body (1) one end waterline sets upper spacer (2), and tank body (1) is another
Hold and lower clapboard (3) is set between waterline and upper spacer (2), water sets slope, lower clapboard (3) slope bottom under lower clapboard (3)
Reserved steam condensate outlet (15).
2. a kind of APG according to claim 1 and the steam flash of alcohol ether glucoside processing fill body device, its feature
It is：Above the end of tank body (1) one end, two liquid level gauge mouths (5) are respectively arranged below, tank body (1) side sets side to examine
Look into manhole (16).
3. a kind of APG according to claim 1 and the steam flash of alcohol ether glucoside processing fill body device, its feature
It is：Tank body (1) bottom side is set up in parallel two heat pump imports (14), standby mouth under heat pump import (14) side is set
(11), tank body (1) bottom opposite side sets steam condensate outlet (15).
4. a kind of APG according to claim 1 and the steam flash of alcohol ether glucoside processing fill body device, its feature
It is：Tank body (1) top center sets heat pump to export (6), and heat pump outlet (6) side sets gradually a upper inspection population respectively
(4), a steam outlet (9), two pressure taps (8), a temperature-measuring port (7)；Heat pump outlet (6) opposite side is set successively respectively
Put a standby mouth (10), a safe valve inlet (12), a steam condensate import (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720833877.8U CN207085368U (en) | 2017-07-10 | 2017-07-10 | A kind of steam flash of APG and alcohol ether glucoside processing fills body device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720833877.8U CN207085368U (en) | 2017-07-10 | 2017-07-10 | A kind of steam flash of APG and alcohol ether glucoside processing fills body device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207085368U true CN207085368U (en) | 2018-03-13 |
Family
ID=61556145
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720833877.8U Expired - Fee Related CN207085368U (en) | 2017-07-10 | 2017-07-10 | A kind of steam flash of APG and alcohol ether glucoside processing fills body device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207085368U (en) |
-
2017
- 2017-07-10 CN CN201720833877.8U patent/CN207085368U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180313 |