CN209791302U - Gelatin concentration ultrafiltration equipment - Google Patents
Gelatin concentration ultrafiltration equipment Download PDFInfo
- Publication number
- CN209791302U CN209791302U CN201920564679.5U CN201920564679U CN209791302U CN 209791302 U CN209791302 U CN 209791302U CN 201920564679 U CN201920564679 U CN 201920564679U CN 209791302 U CN209791302 U CN 209791302U
- Authority
- CN
- China
- Prior art keywords
- gelatin
- outlet
- pipeline
- membrane shell
- raw materials
- 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
- 108010010803 Gelatin Proteins 0.000 title claims abstract description 46
- 229920000159 gelatin Polymers 0.000 title claims abstract description 46
- 239000008273 gelatin Substances 0.000 title claims abstract description 46
- 235000019322 gelatine Nutrition 0.000 title claims abstract description 46
- 235000011852 gelatine desserts Nutrition 0.000 title claims abstract description 46
- 238000000108 ultra-filtration Methods 0.000 title claims abstract description 30
- 239000012528 membrane Substances 0.000 claims abstract description 29
- 239000011521 glass Substances 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 239000002994 raw material Substances 0.000 abstract description 22
- 239000007788 liquid Substances 0.000 abstract description 11
- 238000006243 chemical reaction Methods 0.000 abstract description 5
- 239000010865 sewage Substances 0.000 abstract description 5
- 238000000926 separation method Methods 0.000 abstract description 3
- 230000001105 regulatory effect Effects 0.000 abstract description 2
- 238000010521 absorption reaction Methods 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 abstract 1
- 238000005406 washing Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 102000008186 Collagen Human genes 0.000 description 1
- 108010035532 Collagen Proteins 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 229920001436 collagen Polymers 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 210000002808 connective tissue Anatomy 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 235000013611 frozen food Nutrition 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 235000013402 health food Nutrition 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 210000003205 muscle Anatomy 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 210000003491 skin Anatomy 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000002834 transmittance Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a gelatin concentration ultrafiltration device, which relates to the field of ultrafiltration devices, and comprises a frame, wherein the upper surface of the frame is connected with a feed pump, the outlet of the feed pump is connected with two symmetrical filters through a pipeline, the utility model discloses a, through being provided with the feed pump, gelatin raw materials are injected into the device through the feed pump through the pipeline, then initial pretreatment is carried out through the filter, the raw materials after pretreatment enter a heat exchanger for heat exchange, then the raw materials after heat exchanger conversion enter a circulating pump for absorption and separation through the circulating pump, then the raw materials enter a membrane shell for gelatin concentration ultrafiltration treatment through the outlet of the circulating pump, the raw materials enter an electric regulating ball valve through the outlet of the membrane shell, the raw materials exit from the outlet through an electromagnetic flowmeter and a sight glass, and the gelatin concentration ultrafiltration device is more thorough through multiple steps, the cleaning liquid enters from the liquid inlet to clean the membrane shell, and then the sewage flows out from the liquid outlet.
Description
Technical Field
The utility model relates to an ultrafiltration apparatus field especially relates to concentrated ultrafiltration apparatus of gelatin.
Background
Gelatin is white or yellowish, semitransparent, and slightly lustrous thin sheet or powder particles degraded by collagen in connective tissues such as animal skin, bone, muscle membrane, and sarcodictya; so it is also called animal gelatin and fat glue. The industrial gelatin is colorless to light yellow transparent or semitransparent flakes or particles. No smell and no odor. It is expanded by absorbing water in cold water. Dissolved in hot water. Soluble in glycerol and acetic acid, and insoluble in ethanol and diethyl ether. Gelatin belongs to a macromolecular hydrophilic colloid, is a low-calorie health food with high nutritive value, and can be used for preparing candy additives, frozen food additives and the like. In addition, gelatin is also widely utilized in the pharmaceutical and chemical industries.
in the production process of gelatin, the light transmittance, the color depth, the ash content and the amount of ionic impurities are all influenced by the purity of the gelatin. In order to improve the purity of gelatin, a purification treatment is generally performed to remove particulate and organic impurities from the gelatin solution.
But because traditional concentrated ultrafiltration apparatus of gelatin still has some weak points, the concentrated ultrafiltration apparatus of traditional gelatin is generally more and comparatively complicated to handle the process, often needs higher treatment cost, causes great capital pressure for the production of enterprise, and concentrated ultrafiltration apparatus of gelatin handles simultaneously and exists unable as required selection processing, and consequently the flexibility is lower, and stability is lower, consequently the utility model provides an integrated concentrated ultrafiltration apparatus of gelatin solves above-mentioned problem.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a concentrated ultrafiltration apparatus of gelatin to solve above-mentioned technical problem.
The utility model discloses a solve above-mentioned technical problem, adopt following technical scheme to realize: gelatin concentration ultrafiltration apparatus, which comprises a frame, the upper surface of frame is connected with the charge pump, there are two symmetrical filters in the export of charge pump through the pipe connection, two the export of filter is connected with the heat exchanger through the pipeline jointly, the exit linkage of heat exchanger has the circulating pump, the exit linkage of circulating pump has the membrane shell, there is the electric control ball valve in the exit of membrane shell through the pipe connection, the exit of electric control ball valve is connected with electric control valve, electric control valve's exit is connected with electromagnetic flowmeter, electromagnetic flowmeter's exit is connected with the sight glass.
Preferably, pneumatic butterfly valves are arranged at an inlet and an outlet of the filter, and a diaphragm pressure gauge is arranged on a pipeline on the filter.
Preferably, a pressure transmitter, a diaphragm axial pressure gauge and a temperature transmitter are arranged on a pipeline between the circulating pump and the diaphragm shell.
Preferably, the inlet and the outlet of the membrane shell are provided with a pneumatic ball valve, a pneumatic exhaust ball valve and a check valve.
Preferably, a control cabinet is arranged on the rack.
Preferably, the connection mode between different diameters of the pipeline is eccentric reducing connection.
The utility model has the advantages that:
The utility model discloses in, through being equipped with the charge pump, pass through the charge pump with the gelatin raw materials and pour into among this equipment through the pipeline, then carry out the preliminary treatment in initial stage through the filter, raw materials after the preliminary treatment enter into the heat exchanger and carry out the heat exchange, then the raw materials through the heat exchanger conversion enter into the circulating pump, absorb through the circulating pump, the separation, then enter into through the export of circulating pump and have the membrane shell to carry out gelatin concentration ultrafiltration treatment, the export of raw materials through the membrane shell enters into the electrical control ball valve, come out from the export through electromagnetic flowmeter and sight glass, make gelatin concentration ultrafiltration apparatus more thorough through multiple step, the washing liquid gets into from the inlet, wash the membrane shell, then sewage comes out from the liquid outlet.
Drawings
FIG. 1 is a front view of the gelatin concentrating and ultrafiltering apparatus of the present invention;
FIG. 2 is a top view of the gelatin concentrating and ultrafiltering apparatus of the present invention;
FIG. 3 is a left side view of the gelatin concentrating and ultrafiltering apparatus of the present invention;
Fig. 4 is a right side view of the gelatin concentrating and ultra-filtering device of the present invention.
reference numerals: 1-a feed pump; 2-an electric adjusting ball valve; 3-an electromagnetic flow meter; 4-sight glass; 5-a pneumatic butterfly valve; 6-diaphragm pressure gauge; 7-electric regulating valve; 8-eccentric diameter change; 9-a heat exchanger; 10-a control cabinet; 11-a circulation pump; 12-a pressure transmitter; 13-diaphragm axial pressure gauge; 14-a membrane shell; 15-a temperature transmitter; 16-a pneumatic ball valve; 17-pneumatic vent ball valve; 18-a filter; 19-a check valve; and 20-frame.
Detailed Description
In order to make the technical means, the creation features, the achievement purposes and the functions of the present invention easy to understand, the present invention will be further explained below with reference to the following embodiments and the accompanying drawings, but the following embodiments are only the preferred embodiments of the present invention, and not all embodiments are included. Based on the embodiments in the implementation, other embodiments obtained by those skilled in the art without any creative efforts belong to the protection scope of the present invention.
Specific embodiments of the present invention will be described below with reference to the accompanying drawings.
Example 1
gelatin concentration ultrafiltration equipment, which comprises a frame 20, wherein the upper surface of the frame 20 is connected with a feed pump 1, the outlet of the feed pump 1 is connected with two symmetrical filters 18 through a pipeline, the outlets of the two filters 18 are jointly connected with a heat exchanger 9 through a pipeline, the outlet of the heat exchanger 9 is connected with a circulating pump 11, the outlet of the circulating pump 11 is connected with a membrane shell 14, the outlet of the membrane shell 14 is connected with an electric adjusting ball valve 2 through a pipeline, the outlet of the electric adjusting ball valve 2 is connected with an electric adjusting valve 7, the outlet of the electric adjusting valve 7 is connected with an electromagnetic flowmeter 3, the outlet of the electromagnetic flowmeter 3 is connected with a sight glass 4, a gelatin raw material is injected into the equipment through the pipeline by the feed pump 1 through the feed pump 1, then initial pretreatment is carried out through the filter 18, the pretreated raw material enters the heat, then the raw materials through the conversion of heat exchanger 9 enter into circulating pump 11, absorb, separate through circulating pump 11, then enter into through circulating pump 11 the export have membrane shell 14 to carry out gelatin concentration ultrafiltration treatment, the raw materials enters into electric regulation ball valve 7 through the export of membrane shell 14, come out from the export through electromagnetic flowmeter 3 and sight glass 4, make gelatin concentration ultrafiltration apparatus more thorough through multiple step, the washing liquid gets into from the inlet, go on wasing membrane shell 14, then sewage comes out from the liquid outlet.
Example 2
Gelatin concentration ultrafiltration equipment, which comprises a frame 20, wherein the upper surface of the frame 20 is connected with a feed pump 1, the outlet of the feed pump 1 is connected with two symmetrical filters 18 through a pipeline, the outlets of the two filters 18 are jointly connected with a heat exchanger 9 through a pipeline, the outlet of the heat exchanger 9 is connected with a circulating pump 11, the outlet of the circulating pump 11 is connected with a membrane shell 14, the outlet of the membrane shell 14 is connected with an electric adjusting ball valve 2 through a pipeline, the outlet of the electric adjusting ball valve 2 is connected with an electric adjusting valve 7, the outlet of the electric adjusting valve 7 is connected with an electromagnetic flowmeter 3, the outlet of the electromagnetic flowmeter 3 is connected with a sight glass 4, a gelatin raw material is injected into the equipment through the pipeline by the feed pump 1 through the feed pump 1, then initial pretreatment is carried out through the filter 18, the pretreated raw material enters the heat, then the raw materials through the conversion of heat exchanger 9 enter into circulating pump 11, absorb, separate through circulating pump 11, then enter into through circulating pump 11 the export have membrane shell 14 to carry out gelatin concentration ultrafiltration treatment, the raw materials enters into electric regulation ball valve 7 through the export of membrane shell 14, come out from the export through electromagnetic flowmeter 3 and sight glass 4, make gelatin concentration ultrafiltration apparatus more thorough through multiple step, the washing liquid gets into from the inlet, washs membrane shell 14, then sewage comes out from the liquid outlet.
Pneumatic butterfly valves 5 are arranged at the inlet and the outlet of the filter 18, and a diaphragm pressure gauge 6 is arranged on a pipeline on the filter 18.
And a pressure transmitter 12, a diaphragm axial pressure gauge 13 and a temperature transmitter 15 are arranged on a pipeline between the circulating pump 11 and the diaphragm shell 14.
Pneumatic ball valves 16, pneumatic vent ball valves 17 and check valves 19 are provided at both the inlet and outlet of the membrane housing 14.
The control cabinet 10 is arranged on the frame 20.
The connection mode between the different diameters of the pipelines is eccentric reducing 8 connection.
The working principle is as follows: through being equipped with charge pump 1, inject the gelatin raw materials into this equipment through the pipeline through charge pump 1 in, then carry out initial preliminary treatment through filter 18, raw materials after the preliminary treatment enter into heat exchanger 9 and carry out heat exchange, then the raw materials through heat exchanger 9 conversion enter into circulating pump 11, absorb through circulating pump 11, the separation, then the export through circulating pump 11 enters into to have membrane shell 14 to carry out gelatin concentration ultrafiltration treatment, the export of raw materials through membrane shell 14 enters into electric regulation ball valve 7, come out from the export through electromagnetic flowmeter 3 and sight glass 4, make gelatin concentration ultrafiltration apparatus more thorough through multiple step, the washing liquid enters into from the inlet, wash membrane shell 14, then sewage comes out from the liquid outlet.
In the present disclosure, unless expressly stated or limited otherwise, the first feature "on" or "under" the second feature may comprise direct contact between the first and second features, or may comprise contact between the first and second features not directly. Also, the first feature being "on," "above" and "over" the second feature includes the first feature being directly on and obliquely above the second feature, or merely indicating that the first feature is at a higher level than the second feature. A first feature being "under," "below," and "beneath" a second feature includes the first feature being directly under and obliquely below the second feature, or simply meaning that the first feature is at a lesser elevation than the second feature.
The foregoing shows and describes the general principles, essential features, and advantages of the invention. It should be understood by those skilled in the art that the present invention is not limited by the above embodiments, and the description in the above embodiments and the description is only preferred examples of the present invention, and is not intended to limit the present invention, and that the present invention can have various changes and modifications without departing from the spirit and scope of the present invention, and these changes and modifications all fall into the scope of the claimed invention. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (6)
1. Gelatin concentration ultrafiltration apparatus, including frame (20), its characterized in that: the utility model discloses a solar energy water heater, including frame (20), the upper surface of frame (20) is connected with charge pump (1), the export of charge pump (1) has two symmetrical filter (18), two through the pipe connection the export of filter (18) is connected with heat exchanger (9) jointly through the pipeline, the exit linkage of heat exchanger (9) has circulating pump (11), the exit linkage of circulating pump (11) has membrane shell (14), there are electric regulation ball valve (2) in the exit of membrane shell (14) through the pipe connection, the exit of electric regulation ball valve (2) is connected with electric regulation valve (7), the exit of electric regulation valve (7) is connected with electromagnetic flowmeter (3), the exit of electromagnetic flowmeter (3) is connected with sight glass (4).
2. The gelatin concentrating ultrafiltration apparatus of claim 1, wherein: pneumatic butterfly valves (5) are arranged at an inlet and an outlet of the filter (18), and a diaphragm pressure gauge (6) is arranged on a pipeline on the filter (18).
3. The gelatin concentrating ultrafiltration apparatus of claim 1, wherein: and a pressure transmitter (12), a diaphragm axial pressure gauge (13) and a temperature transmitter (15) are arranged on a pipeline between the circulating pump (11) and the membrane shell (14).
4. The gelatin concentrating ultrafiltration apparatus of claim 1, wherein: and a pneumatic ball valve (16), a pneumatic exhaust ball valve (17) and a check valve (19) are arranged at the inlet and the outlet of the membrane shell (14).
5. The gelatin concentrating ultrafiltration apparatus of claim 1, wherein: the rack (20) is provided with a control cabinet (10).
6. The gelatin concentrating ultrafiltration apparatus of claim 1, wherein: the connecting mode among the different diameters of the pipeline is eccentric reducing (8) connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920564679.5U CN209791302U (en) | 2019-04-24 | 2019-04-24 | Gelatin concentration ultrafiltration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920564679.5U CN209791302U (en) | 2019-04-24 | 2019-04-24 | Gelatin concentration ultrafiltration equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209791302U true CN209791302U (en) | 2019-12-17 |
Family
ID=68830775
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920564679.5U Expired - Fee Related CN209791302U (en) | 2019-04-24 | 2019-04-24 | Gelatin concentration ultrafiltration equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209791302U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113441011A (en) * | 2021-07-20 | 2021-09-28 | 合肥科锐特环保工程有限公司 | Gelatin film treatment facility |
-
2019
- 2019-04-24 CN CN201920564679.5U patent/CN209791302U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113441011A (en) * | 2021-07-20 | 2021-09-28 | 合肥科锐特环保工程有限公司 | Gelatin film treatment facility |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191217 |