CN213050144U - Mixing system is thrown to liquifying enzyme - Google Patents
Mixing system is thrown to liquifying enzyme Download PDFInfo
- Publication number
- CN213050144U CN213050144U CN202021362555.8U CN202021362555U CN213050144U CN 213050144 U CN213050144 U CN 213050144U CN 202021362555 U CN202021362555 U CN 202021362555U CN 213050144 U CN213050144 U CN 213050144U
- Authority
- CN
- China
- Prior art keywords
- pipe
- enzyme
- tank
- proportioning
- pipe portion
- 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.)
- Active
Links
Images
Abstract
The utility model relates to a liquefying enzyme adding and mixing system, which comprises a size mixing device and an enzyme adding device, wherein the size mixing device comprises a proportioning tank, a feeding tank, a proportioning pipe, a transfer pump arranged on the proportioning pipe, a mixer arranged on the proportioning pipe between the transfer pump and the feeding tank, and an acid adding component communicated with the mixer; the blender includes first pipe portion, set up on first pipe portion and the feed inlet that is linked together with the upper reaches of batching pipe, be linked together and extending direction and the extending direction looks vertically second pipe portion of first pipe portion with first pipe portion, set up on the second pipe portion and with the acid feeding mouth that the subassembly is linked together, with first pipe portion be linked together and the biggest internal diameter is greater than the third pipe portion of the biggest internal diameter of first pipe portion, set up on the third pipe portion and the discharge gate that is linked together with the low reaches of batching pipe. The utility model discloses an adopt the blender of particular structure, can make starch thick liquid and sour more even of mixing to be favorable to going on of follow-up reaction.
Description
Technical Field
The utility model relates to a compounding system is thrown to liquefaction enzyme.
Background
Mixing starch slurry and acid among the prior art utilizes starch slurry and sour whirl etc. that form when circulating in the pipeline to carry out automatic mixing usually, however, this kind of mixing mode is difficult to control to there may be starch slurry and the inhomogeneous problem of acid mixing, thereby lead to starch slurry and acid still not to mix evenly in the material loading jar, and be unfavorable for follow-up liquefaction reaction, thereby lead to the unstable problem of product.
Disclosure of Invention
The utility model aims at providing a can make starch slurry and sour misce bene's liquefaction enzyme throw and add compounding system.
In order to achieve the above purpose, the utility model adopts the technical scheme that:
a liquefying enzyme feeding and mixing system comprises a size mixing device and an enzyme adding device for adding liquefying enzyme into the size mixing device, wherein the size mixing device comprises a proportioning tank, a feeding tank, a proportioning pipe for communicating the proportioning tank with the feeding tank, a transfer pump arranged on the proportioning pipe, a mixer arranged on the proportioning pipe between the transfer pump and the feeding tank, and an acid adding component communicated with the mixer; the blender include first pipe portion, set up first pipe portion on and with the upper reaches of batching pipe feed inlet that is linked together, with first pipe portion be linked together and extending direction with the extending direction looks vertically second pipe portion of first pipe portion, set up the second pipe portion on and with the acid feeding subassembly advance sour mouthful that is linked together, with first pipe portion be linked together and the maximum internal diameter is greater than the maximum internal diameter's of first pipe portion third pipe portion on and with the discharge gate that the low reaches of batching pipe are linked together.
The utility model discloses an installation has the blender of particular structure on the batching pipe between transfer pump and material loading jar to avoid because starch thick liquid and the inhomogeneous unstable problem of product that leads to of acid mixture.
The utility model discloses in, first pipe portion second pipe portion third pipe portion be a whole, can be through welded mode fixed connection, also can once mould the tee bend structure that the type formed to preferably use acid and alkali-resistance's material.
Preferably, the first pipe part comprises an outer pipe with one end provided with the feed port, a first inner pipe which is positioned in the outer pipe and has an opening facing the opposite side of the feed port, and a second inner pipe which is positioned in the outer pipe and has an opening facing the feed port, a gap is formed between the free end part of the first inner pipe and the free end part of the second inner pipe, the center of the gap is positioned on the axis of the second pipe part, the second pipe part is connected with the outer pipe, and the third pipe part is connected with the other end of the outer pipe.
Furthermore, the cross section of the first inner pipe is gradually reduced from the feeding hole to the discharging hole, one end of the first inner pipe is fixedly connected with the inner wall of the outer pipe, the inner diameter of the cross section where the free end of the first inner pipe is located is 0.5-0.6 times of the inner diameter of the outer pipe, and the length of the first inner pipe is 0.15-0.25 times of the total length of the outer pipe.
Furthermore, the second inner pipe comprises a first part in a cylindrical shape and a second part, and two ends of the second part are fixedly connected with the first part and the joint of the outer pipe and the third pipe part respectively; the inner diameter of the first part is 0.72-0.82 times of the inner diameter of the outer pipe, and the length of the first part is 0.1-0.2 times of the total length of the outer pipe; the cross section of the second part is gradually increased from the feeding hole to the discharging hole, and the length of the second part is 0.15-0.25 times of the total length of the outer pipe.
Further, the distance between the free end of the first inner pipe and the free end of the second inner pipe is 0.05-0.1 times of the total length of the outer pipe.
Preferably, the third pipe portion comprises a third portion having one end fixedly connected to the first pipe portion, a fourth portion having one end fixedly connected to the other end of the third portion, a fifth portion having one end fixedly connected to the other end of the fourth portion, and a sixth portion having one end fixedly connected to the other end of the fifth portion, and the discharge hole is formed at the other end of the sixth portion; the cross section of the third part is gradually increased from the feed inlet to the discharge outlet; the fourth part is cylindrical, and the inner diameter of the fourth part is 1.5-1.6 times of the inner diameter of the cross section where the third part is connected with the first pipe part; the cross section of the fifth part is gradually reduced from the feed inlet to the discharge outlet; the sixth part is cylindrical, and the inner diameter of the sixth part is the same as the inner diameter of the cross section of the joint of the third part and the first pipe part; the length ratio of the third part to the fourth part is 1 (1.1-1.3); the length ratio of the third part to the fifth part is 1 (0.9-1.1); the length ratio of the third part to the sixth part is 1 (1.1-1.3); the ratio of the total length of the third pipe part to the total length of the first pipe part is (1.3-1.4): 1.
The utility model discloses a blender can make the feed liquid get into the space through first inner tube, and the acidizing fluid joins with the feed liquid in getting into the space through the second body to along with the feed liquid gets into third pipe portion, further misce bene in the third pipe portion.
According to a specific embodiment, the size mixing device is located in a first chamber, the enzyme adding device is located in a second chamber, the first chamber and the second chamber are independently arranged, and the second chamber is a constant-temperature chamber. The utility model discloses an it installs in the thermostatic chamber to add the enzyme device to workshop high temperature has been avoided to the influence of enzyme.
According to a specific embodiment, the liquefying enzyme adding and mixing system further comprises an automatic control system capable of controlling the size mixing device and the enzyme adding device; the size mixing device also comprises a mass flow meter arranged on a batching pipe between the mixer and the feeding tank; the enzyme adding device comprises an electronic scale positioned in the second chamber, an enzyme tank arranged on the electronic scale, an enzyme adding pipe respectively communicated with the enzyme tank and the size mixing device, and an enzyme adding pump assembly arranged on the enzyme adding pipe; the electronic scale, the enzyme adding pump assembly, the mass flow meter and the transfer pump are respectively connected with the automatic control system, the mass flow meter is interlocked with the enzyme adding pump assembly, and the transfer pump is interlocked with the mass flow meter; the enzyme adding pipe is communicated with the feeding tank.
According to a specific and preferred embodiment, said mixing apparatus further comprises a alkalizing assembly in communication with the batching pipe between said batching tank and said transfer pump; the alkali adding assembly comprises an alkali adding pipe communicated with the batching pipe and an alkali adding pump assembly arranged on the alkali adding pipe, and the alkali adding pump assembly is interlocked with the mass flowmeter; the acid adding assembly comprises an acid adding pipe communicated with the batching pipe and an acid adding pump assembly arranged on the acid adding pipe, and the acid adding pump assembly is interlocked with the mass flowmeter.
The utility model discloses in, the alkali pump subassembly with the acidification pump subassembly all with automatic control system be connected. The pH can be adjusted on line and automatically by adding acid and alkali through the use of an automatic control system.
Preferably, the alkali-adding component and the acid-adding pump component are both made of acid-alkali resistant materials.
According to a specific implementation mode, the liquefying enzyme feeding and mixing system further comprises a condensate pipe communicated with the batching tank and the feeding tank, and a primary water pipe communicated with the batching tank and the batching pipe between the transfer pumps.
The utility model discloses in, automatic control system uses is the DCS system. The on-line and automatic enzyme adding can be realized by using an automatic control system.
Preferably, the automatic control system is installed in the third room, i.e., the central control room, so as to facilitate monitoring by an operator.
Because of the application of the technical scheme, compared with the prior art, the utility model has the following advantages:
the utility model discloses an adopt the blender of particular structure, can make starch thick liquid and sour more even of mixing to be favorable to going on of follow-up reaction.
Drawings
FIG. 1 is a schematic structural diagram of a liquefying enzyme adding and mixing system according to an embodiment of the present invention;
FIG. 2 is a schematic structural diagram of a mixer according to an embodiment of the present invention;
in the attached figure 1:1. a first chamber; 111. a dosing tank; 112. a first batching pipe; 113. a transfer pump; 114. a second batching pipe; 115. a mixer; 116. a third batching pipe; 117. a mass flow meter; 118. feeding the material tank; 119. adding an acid pipe; 120. an acid pump assembly; 121. adding an alkali tube; 122. a base pump assembly; 123. a first condensate pipe; 124. a second condensate pipe; 125. a primary water pipe; 126. a feeding pipe; 2. A second chamber; 211. an electronic scale; 212. an enzyme tank; 213. a first enzyme adding tube; 214. adjusting a valve; 215. adding an enzyme pump; 216. a second enzyme adding tube; 217. a three-way valve; 218. a flow meter; 219. a third enzyme adding tube; 220. a return pipe;
in the attached fig. 2: 11. a feed inlet; 12. an outer tube; 13. a first inner tube; 14. a first portion; 15. a second portion; 21. a second pipe portion; 22. an acid inlet; 31. a third portion; 32. a fourth part; 33. a fifth part; 34. a sixth section; 35. and (4) a discharge port.
Detailed Description
The invention will be further described with reference to the embodiments shown in fig. 1 and 2.
The liquefying enzyme adding and mixing system shown in figure 1 comprises a size mixing device and an enzyme adding device.
The slurry mixing device comprises a proportioning tank 111, a feeding tank 118, a proportioning pipe for communicating the proportioning tank 111 with the feeding tank 118, a transfer pump 113 installed on the proportioning pipe, a mixer 115 installed on the proportioning pipe between the transfer pump 113 and the feeding tank 118, and an acid adding assembly communicated with the mixer 115.
The top of batching jar 111 is linked together with supplied materials pipe 126, and the top of batching jar 111 still is linked together with first condensate pipe 123, and the bottom of batching jar 111 is linked together with the batching pipe.
The batching pipe comprises a first batching pipe 112, the mixing device comprises a second proportioning pipe 114 and a third proportioning pipe 116, wherein one end of the first proportioning pipe 112 is communicated with the bottom of the proportioning tank 111, the other end of the first proportioning pipe 112 is communicated with a feeding hole of a transfer pump 113, the first proportioning pipe 112 is further communicated with a primary water pipe 125, the first proportioning pipe 112 between the primary water pipe 125 and the transfer pump 113 is further communicated with an alkali adding pipe 121 provided with an alkali adding pump assembly 122, a discharging hole of the transfer pump 113 is communicated with one end of the second proportioning pipe 114, the other end of the second proportioning pipe 114 is communicated with a feeding hole 11 of a mixer 115, an acid inlet 22 of the mixer 115 is communicated with an acid adding pipe 119 provided with an acid adding pump assembly 120, a discharging hole 35 of the mixer 115 is communicated with one end of the third proportioning pipe 116, a mass flow meter 117 is arranged on the third proportioning pipe 116, and the other end of the third proportioning pipe 116 is communicated with the top of an upper charging tank 118.
As shown in fig. 2, the mixer 115 includes a first pipe portion, a second pipe portion 21, and a third pipe portion.
The first pipe part comprises an outer pipe 12 with one end provided with a feed inlet 11, a first inner pipe 13 and a second inner pipe which are positioned in the outer pipe 12. The opening of the first inner pipe 13 faces to the opposite side of the feed port 11, the cross section is gradually reduced from the feed port 11 to the discharge port 35, one end (the end close to the feed port 11) of the first inner pipe 13 is fixedly connected with the inner wall of the outer pipe 12, the inner diameter of the cross section where the free end of the first inner pipe 13 is located is 0.5-0.6 times, preferably 0.56 times, the inner diameter of the outer pipe 12, and the length of the first inner pipe 13 is 0.15-0.25 times, preferably 0.2 times, the total length of the outer pipe 12; the opening of the second inner pipe faces the feed inlet 11, the second inner pipe comprises a first part 14 and a second part 15, the first part 14 is cylindrical, the inner diameter of the first part 14 is 0.72-0.82 times, preferably 0.79 times, the inner diameter of the outer pipe 12, and the length of the first part 14 is 0.1-0.2 times, preferably 0.14 times, the total length of the outer pipe 12; one end of the second part 15 is fixedly connected with one end of the first part 14, the other end of the second part 15 is fixedly connected with the joint of the outer pipe 12 and the third pipe part, the cross section of the second part 15 is gradually increased from the feed port 11 to the discharge port 35, and the length of the second part 15 is 0.15-0.25 times, preferably 0.2 times, of the total length of the outer pipe 12. A gap is formed between the free end of the first inner tube 13 and the free end of the first portion 14 of the second inner tube, and the distance between the free end of the first inner tube 13 and the free end of the second inner tube is 0.05 to 0.1 times, preferably 0.09 times, the total length of the outer tube 12.
One end of the second pipe part 21 is communicated with the first pipe part, the extending direction of the second pipe part is vertical to the extending direction of the first pipe part, the axial lead of the second pipe part 21 is coincided with the central line of a gap between the free end part of the first inner pipe 13 and the free end part of the second inner pipe, the distance between the free end part of the first inner pipe 13 and the free end part of the second inner pipe is smaller than the inner diameter of the second pipe part 21, the other end of the second pipe part 21 is provided with an acid inlet 22, and the acid inlet 22 is communicated with an acid adding pipe 119 provided with an acid adding pump component 120.
The third tube part comprises a third portion 31, a fourth portion 32, a fifth portion 33 and a sixth portion 34. One end of the third part 31 is fixedly connected with the first pipe part, the other end of the third part 31 is fixedly connected with one end of the fourth part 32, the other end of the fourth part 32 is fixedly connected with one end of the fifth part 33, the other end of the fifth part 33 is fixedly connected with one end of the sixth part 34, and the other end of the sixth part 34 is provided with a discharge hole 35 communicated with the third batching pipe 116; the cross section of the third part 31 is gradually increased from the feed inlet 11 to the discharge outlet 35; the fourth part 32 is cylindrical, and the inner diameter of the fourth part 32 is 1.5-1.6 times, preferably 1.56 times, that of the cross section where the third part 31 is connected with the first pipe part; the cross section of the fifth part 33 is gradually reduced from the feed inlet 11 to the discharge outlet 35; the sixth part 34 is cylindrical, and the inner diameter of the sixth part 34 is the same as the inner diameter of the cross section where the third part 31 is connected with the first pipe part; the length ratio of the third part 31 to the fourth part 32 is 1 (1.1-1.3), preferably 1: 1.2; the length ratio of the third part 31 to the fifth part 33 is 1 (0.9-1.1), and the preferred length ratio is 1: 1; the length ratio of the third part 31 to the sixth part 34 is 1 (1.1-1.3), preferably 1: 1.2; the ratio of the total length of the third pipe part to the total length of the first pipe part is (1.3-1.4): 1, and the preferred length ratio is 1.35: 1.
The top of the feeding tank 118 is also communicated with one end of a second condensed water pipe 124, and the other end of the second condensed water pipe 124 is communicated with a first condensed water pipe 123.
The enzyme adding device comprises an electronic scale 211 positioned in the second chamber 2, an enzyme tank 212 arranged on the electronic scale 211, an enzyme adding pipe respectively communicated with the enzyme tank 212 and the size mixing device, and an enzyme adding pump assembly arranged on the enzyme adding pipe.
The enzyme adding pump assembly comprises an enzyme adding pump 215 arranged on an enzyme adding pipe, a regulating valve 214, a three-way valve 217 positioned at the downstream of the enzyme adding pump 215 and a flow meter 218 positioned at the downstream of the three-way valve 217; the enzyme adding device also comprises a return pipe 220 which is respectively communicated with the three-way valve 217 and the interior of the enzyme tank 212.
The enzyme tank 212 is communicated with a first enzyme adding pipe 213, the first enzyme adding pipe 213 is provided with an adjusting valve 214, the other end of the first enzyme adding pipe 213 is communicated with an enzyme inlet of an enzyme adding pump 215, an enzyme outlet of the enzyme adding pump 215 is communicated with a second enzyme adding pipe 216, the other end of the second enzyme adding pipe 216 is communicated with a three-way valve 217, the three-way valve 217 is communicated with a third enzyme adding pipe 219 provided with a flow meter 218 and the adjusting valve 214, the other end of the third enzyme adding pipe 219 is communicated with the upper end of the feeding tank 118, the three-way valve 217 is also communicated with one end of a return pipe 220, and the other end of the return pipe 220 is communicated with the upper end inside the enzyme tank 212.
In this embodiment, the enzyme pump assembly, the transit pump 113, the acid pump assembly 120, and the alkali pump assembly 122 are interlocked with the mass flow meter 117; the electronic scale 211, the enzyme pump assembly, the transfer pump 113, the acid pump assembly 120, the base pump assembly 122 and the mass flow meter 117 are connected to an automatic control system.
In this embodiment, the size mixing device is located in the first chamber 1, the enzyme adding device is located in the second chamber 2, the first chamber 1 and the second chamber 2 are independently arranged, and the second chamber 2 is a constant temperature chamber.
In this embodiment, the alkali-adding component and the acid-adding pump component 120 are made of acid-base resistant materials.
In this embodiment, the automatic control system uses a DCS system.
In this embodiment, the automatic control system is installed in the third room, i.e., the central control room, so that the monitoring by the operator is facilitated.
The above embodiments are only for illustrating the technical concept and features of the present invention, and the purpose of the embodiments is to enable people skilled in the art to understand the contents of the present invention and to implement the present invention, which cannot limit the protection scope of the present invention. All equivalent changes and modifications made according to the spirit of the present invention should be covered by the protection scope of the present invention.
Claims (10)
1. The utility model provides a liquefaction enzyme throws with compounding system, including the size mixing device and to the size mixing device add the enzyme device that adds of liquefaction enzyme, its characterized in that: the slurry mixing device comprises a proportioning tank (111), a feeding tank (118), a proportioning pipe for communicating the proportioning tank (111) with the feeding tank (118), a transfer pump (113) arranged on the proportioning pipe, a mixer (115) arranged on the proportioning pipe between the transfer pump (113) and the feeding tank (118), and an acid adding component communicated with the mixer (115); mixer (115) include first pipe portion, set up first pipe portion on and with feed inlet (11) that the upper reaches of batching pipe be linked together, with first pipe portion be linked together and extending direction with extending direction looks vertically second pipe portion (21) of first pipe portion, set up second pipe portion (21) on and with acid feeding component be linked together advance sour mouth (22), with first pipe portion be linked together and the maximum internal diameter be greater than the maximum internal diameter's of first pipe portion third pipe portion, set up third pipe portion on and with the discharge gate (35) that the lower reaches of batching pipe are linked together.
2. The liquefying enzyme dosing and mixing system according to claim 1, wherein: the first pipe part comprises an outer pipe (12) with one end provided with the feed inlet (11), a first inner pipe (13) which is positioned in the outer pipe (12) and has an opening facing the opposite side of the feed inlet (11), and a second inner pipe which is positioned in the outer pipe (12) and has an opening facing the feed inlet (11), wherein a gap is formed between the free end part of the first inner pipe (13) and the free end part of the second inner pipe, the center of the gap is positioned on the axis of the second pipe part (21), the second pipe part (21) is connected with the outer pipe (12), and the third pipe part is connected with the other end of the outer pipe (12).
3. The liquefying enzyme dosing and mixing system according to claim 2, wherein: the cross section of the first inner pipe (13) is gradually reduced from the feeding hole (11) to the discharging hole (35), one end of the first inner pipe (13) is fixedly connected with the inner wall of the outer pipe (12), the inner diameter of the cross section where the free end of the first inner pipe (13) is located is 0.5-0.6 times of the inner diameter of the outer pipe (12), and the length of the first inner pipe (13) is 0.15-0.25 times of the total length of the outer pipe (12).
4. The liquefying enzyme dosing and mixing system according to claim 2, wherein: the second inner pipe comprises a first cylindrical part (14) and a second part (15) of which two ends are fixedly connected with the first part (14) and the joint of the outer pipe (12) and the third pipe part respectively; the inner diameter of the first part (14) is 0.72-0.82 times of the inner diameter of the outer pipe (12), and the length of the first part (14) is 0.1-0.2 times of the total length of the outer pipe (12); the cross section of the second part (15) is gradually increased from the feed inlet (11) to the discharge outlet (35), and the length of the second part (15) is 0.15-0.25 times of the total length of the outer pipe (12).
5. The liquefying enzyme dosing and mixing system according to claim 2, wherein: the distance between the free end of the first inner pipe (13) and the free end of the second inner pipe is 0.05-0.1 times of the total length of the outer pipe (12).
6. The liquefying enzyme dosing and mixing system according to claim 1, wherein: the third pipe part comprises a third part (31) with one end fixedly connected with the first pipe part, a fourth part (32) with one end fixedly connected with the other end of the third part (31), a fifth part (33) with one end fixedly connected with the other end of the fourth part (32), and a sixth part (34) with one end fixedly connected with the other end of the fifth part (33), and the discharge hole (35) is arranged at the other end of the sixth part (34); the cross section of the third part (31) is gradually increased from the feed inlet (11) to the discharge outlet (35); the fourth part (32) is cylindrical, and the inner diameter of the fourth part (32) is 1.5-1.6 times of the inner diameter of the cross section where the third part (31) is connected with the first pipe part; the cross section of the fifth part (33) is gradually reduced from the feed inlet (11) to the discharge outlet (35); the sixth part (34) is cylindrical, and the inner diameter of the sixth part (34) is the same as the inner diameter of the cross section of the joint of the third part (31) and the first pipe part; the length ratio of the third part (31) to the fourth part (32) is 1 (1.1-1.3); the length ratio of the third part (31) to the fifth part (33) is 1 (0.9-1.1); the length ratio of the third part (31) to the sixth part (34) is 1 (1.1-1.3); the ratio of the total length of the third pipe part to the total length of the first pipe part is (1.3-1.4): 1.
7. The liquefying enzyme dosing and mixing system according to claim 1, wherein: the size mixing device is positioned in a first chamber (1), the enzyme adding device is positioned in a second chamber (2), the first chamber (1) and the second chamber (2) are independently arranged, and the second chamber (2) is a constant-temperature chamber.
8. The liquefying enzyme dosing and mixing system according to claim 7, wherein: the liquefying enzyme adding and mixing system also comprises an automatic control system which can control the size mixing device and the enzyme adding device; the slurry mixing device also comprises a mass flow meter (117) arranged on a batching pipe between the mixer (115) and the feeding tank (118); the enzyme adding device comprises an electronic scale (211) positioned in the second chamber (2), an enzyme tank (212) arranged on the electronic scale (211), an enzyme adding pipe respectively communicated with the enzyme tank (212) and the size mixing device, and an enzyme adding pump assembly arranged on the enzyme adding pipe; the electronic scale (211), the enzyme adding pump assembly, the mass flow meter (117) and the transfer pump (113) are respectively connected with the automatic control system, the mass flow meter (117) is interlocked with the enzyme adding pump assembly, and the transfer pump (113) is interlocked with the mass flow meter (117); the enzyme adding pipe is communicated with the feeding tank (118).
9. The liquefying enzyme dosing and mixing system according to claim 8, wherein: the size mixing device also comprises an alkali adding component communicated with a batching pipe between the batching tank (111) and the transfer pump (113); the alkali adding assembly comprises an alkali adding pipe (121) communicated with the batching pipe and an alkali adding pump assembly (122) arranged on the alkali adding pipe (121), and the alkali adding pump assembly (122) is interlocked with the mass flow meter (117); the acid adding assembly comprises an acid adding pipe (119) communicated with the batching pipe and an acid adding pump assembly (120) arranged on the acid adding pipe (119), wherein the acid adding pump assembly (120) is interlocked with the mass flow meter (117).
10. The liquefying enzyme dosing and mixing system according to claim 8, wherein: the liquefying enzyme dosing and mixing system further comprises a proportioning tank (111) and a condensate pipe communicated with the feeding tank (118), and a primary water pipe (125) communicated with the proportioning tank (111) and the proportioning pipe between the transfer pumps (113).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021362555.8U CN213050144U (en) | 2020-07-13 | 2020-07-13 | Mixing system is thrown to liquifying enzyme |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021362555.8U CN213050144U (en) | 2020-07-13 | 2020-07-13 | Mixing system is thrown to liquifying enzyme |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN213050144U true CN213050144U (en) | 2021-04-27 |
Family
ID=75572381
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021362555.8U Active CN213050144U (en) | 2020-07-13 | 2020-07-13 | Mixing system is thrown to liquifying enzyme |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN213050144U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114410713A (en) * | 2022-02-14 | 2022-04-29 | 双桥（厦门）有限公司 | Method and device for preparing starch syrup by using corn |
| CN114517217A (en) * | 2022-03-17 | 2022-05-20 | 中诺生物科技发展江苏有限公司 | Preparation method and device of fructo-oligosaccharide with high kestose content |
-
2020
- 2020-07-13 CN CN202021362555.8U patent/CN213050144U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114410713A (en) * | 2022-02-14 | 2022-04-29 | 双桥（厦门）有限公司 | Method and device for preparing starch syrup by using corn |
| CN114410713B (en) * | 2022-02-14 | 2024-07-05 | 双桥（厦门）有限公司 | Method and device for preparing starch syrup by using corn |
| CN114517217A (en) * | 2022-03-17 | 2022-05-20 | 中诺生物科技发展江苏有限公司 | Preparation method and device of fructo-oligosaccharide with high kestose content |
| CN114517217B (en) * | 2022-03-17 | 2023-11-24 | 中诺生物科技发展江苏有限公司 | Preparation method and device of fructo-oligosaccharide with high content of kestose |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN213050144U (en) | Mixing system is thrown to liquifying enzyme | |
| CN112757493A (en) | Liquid metering device, stirring station and liquid metering control method | |
| CN210855314U (en) | Sewage treatment adds medicament device | |
| CN209320017U (en) | A kind of concrete admixture automatic adding device applied on tank car | |
| CN206526745U (en) | For producing the energy-saving automatic batch mixing stirred tank of water reducer | |
| CN212942767U (en) | Liquefying enzyme dosing system | |
| CN214514299U (en) | Liquid preparation system | |
| CN205528471U (en) | Polycarboxylate water reducing agent means of sediment production system of area spraying dry powder device | |
| CN108654542A (en) | A kind of modified asphalt waterproof coiled material continuous batching device and distribution | |
| CN211216215U (en) | Full-automatic methanol gasoline continuous blending equipment | |
| CN220677721U (en) | Immediate preparation system for lactic acid solution | |
| CN209351957U (en) | A kind of spiral heating formula measuring tank | |
| CN208554182U (en) | A kind of integrated form polycarboxylate water-reducer production equipment | |
| CN221386373U (en) | Phenolic resin production system | |
| CN217910251U (en) | Automatic proportioning device of emulsion | |
| CN216884467U (en) | 3D prints online extrusion device that mixes of cement-based material | |
| CN214973245U (en) | Device for preparing different medicaments | |
| CN204746302U (en) | Tank reactor's overflow feed arrangement | |
| CN220386460U (en) | Automatic quantitative feed slurry mixing device | |
| CN215150489U (en) | Auxiliary material prefabrication and automatic device that adds that gypsum board was used | |
| CN219291419U (en) | Novel chemical raw material low-temperature reaction kettle | |
| CN221171277U (en) | Valve array system | |
| CN220194750U (en) | Three-cavity type automatic medicine feeding device | |
| CN217834181U (en) | Storage barrel for concrete additive weighing system | |
| CN212554440U (en) | Production of reinforced concrete pipe is with mixing mixer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |