CN114457199A - Combined crystallizing tank for polycrystalline rock sugar - Google Patents
Combined crystallizing tank for polycrystalline rock sugar Download PDFInfo
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- CN114457199A CN114457199A CN202210316159.9A CN202210316159A CN114457199A CN 114457199 A CN114457199 A CN 114457199A CN 202210316159 A CN202210316159 A CN 202210316159A CN 114457199 A CN114457199 A CN 114457199A
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- 235000000346 sugar Nutrition 0.000 title claims abstract description 68
- 239000011435 rock Substances 0.000 title claims abstract description 35
- 238000002425 crystallisation Methods 0.000 claims abstract description 137
- 230000008025 crystallization Effects 0.000 claims abstract description 136
- 239000007788 liquid Substances 0.000 claims description 23
- 229910001220 stainless steel Inorganic materials 0.000 claims description 8
- 239000010935 stainless steel Substances 0.000 claims description 8
- 238000005452 bending Methods 0.000 claims description 3
- 235000009508 confectionery Nutrition 0.000 claims description 2
- 235000021551 crystal sugar Nutrition 0.000 abstract description 51
- 238000000034 method Methods 0.000 abstract description 21
- 230000008569 process Effects 0.000 abstract description 19
- 238000004519 manufacturing process Methods 0.000 abstract description 17
- 230000006872 improvement Effects 0.000 abstract description 4
- 239000013078 crystal Substances 0.000 description 46
- 210000005056 cell body Anatomy 0.000 description 11
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 230000009286 beneficial effect Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 235000021552 granulated sugar Nutrition 0.000 description 3
- 230000033001 locomotion Effects 0.000 description 3
- 230000001154 acute effect Effects 0.000 description 2
- 239000003086 colorant Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229930006000 Sucrose Natural products 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000002671 adjuvant Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000003599 food sweetener Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 235000012907 honey Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 235000014101 wine Nutrition 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B30/00—Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
- C13B30/02—Crystallisation; Crystallising apparatus
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- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
- Peptides Or Proteins (AREA)
Abstract
The invention belongs to the technical field of crystal sugar crystallization, and particularly relates to a combined crystallization tank for polycrystalline crystal sugar, which comprises a W-shaped tank body and a V-shaped piece; two crystallizing tank cavities are arranged on the W-shaped tank body; the two crystallizing tank cavities are long grooves which are transversely parallel, and the notch of each crystallizing tank cavity is flared and arranged upwards; at least one V-shaped piece is arranged in each crystallization groove cavity in an inverted manner, the surface of each V-shaped piece and the wall surface of each crystallization groove cavity are smooth, and an attachment point is provided for crystallization of the polycrystalline rock sugar. Utilize the crystallizer of W shape in this scheme, at first can effectual promotion crystal sugar crystallization rate, crystallization efficiency promotes more than 25%, and the wall that this crystallizer structure is used for the crystallization moreover can make the product quality have very big improvement, has solved current polycrystal crystal sugar production crystallization process, and is long consuming time, and the crystallization is slow, the problem that the yield is low, uses this technique back, the effectual above-mentioned current situation that has changed, makes the product have bigger competitiveness.
Description
Technical Field
The invention belongs to the technical field of crystal sugar crystallization, and particularly relates to a combined crystallization tank for polycrystalline crystal sugar.
Background
The crystal sugar is an ice-cube-shaped crystal formed by decocting white granulated sugar, and comprises a single crystal and a polycrystal, and both the single crystal and the polycrystal are transparent or semitransparent. The crystal sugar is a crystal reproduced product of granulated sugar, the naturally generated crystal sugar has white, yellowish, light grey and other colors, and various colored crystal sugars with edible pigments, such as green, blue, orange, reddish, dark red and other colors, are also available in the market.
The single crystal rock sugar is a regular transparent crystal, is a novel rock sugar produced in the sixties of the last century, and has the following production process: dissolving white sugar in appropriate amount of water under heating, filtering, introducing into a crystallizing tank to make sugar solution supersaturated, adding seed crystal for crystal growth, taking out after crystal growth, removing Mel, centrifuging, drying, sieving, and grading. The polycrystal crystal sugar is prepared by purifying and dissolving granulated sugar and then crystallizing, and has pure quality and difficult deterioration, so that the polycrystal crystal sugar can be used as a high-grade food sweetening agent, a prepared medicine for soaking wines, nourishing adjuvants and the like besides being eaten as a candy, and has very wide application. At present, the honey pouring of the polycrystal rock sugar crystallizing trolley adopts manual operation, so that the polycrystal rock sugar can be contacted inevitably, the quality of a product is influenced, the manual labor intensity is high, and the production efficiency is low.
The production of domestic crystal sugar generally adopts a traditional technology, be promptly under high temperature the sugar liquid concentration, then make natural cooling, in cooling process, the crystal sugar just progressively crystallizes out from the supersaturated sugar liquid, the crystallization of crystal sugar is with hot saturated sugar liquid cooling back, the sugar leads to the sugar liquid supersaturation because of the solubility reduces, thereby the sugar is separated out with the form of crystal, thereby the crystallization forms the ice sugar piece, traditional crystal sugar crystallization device is very inconvenient when taking out the ice sugar piece that the crystallization formed, need spend more time and energy.
In the production process of crystal sugar, the crystallization process of crystal sugar directly influences the product quality of polycrystal crystal sugar, probably causes the problem that the crystal is loose, the yield is not high etc. and the crystallization process of polycrystal crystal sugar will directly be influenced to the structure of crystallizer, and for the crystallization process of crystal sugar, it is necessary to design a crystallizer structure that can improve polycrystal crystal sugar yield and product quality.
Disclosure of Invention
In order to solve the problems that the yield of polycrystalline rock sugar produced by crystallization of the existing crystallization tank structure is not high, the product quality is lower, the crystal structure is loose, the crystallization speed is low and the like, the scheme provides a combined crystallization tank for polycrystalline rock sugar.
The technical scheme adopted by the invention is as follows:
a combined crystallizing tank for polycrystalline rock sugar comprises a W-shaped tank body and a V-shaped piece;
two crystallizing tank cavities are arranged on the W-shaped tank body; the two crystallizing tank cavities are long grooves which are transversely parallel, and the notch of each crystallizing tank cavity is flared and arranged upwards;
at least one V-shaped piece is arranged in each crystallization groove cavity in an inverted manner, the surface of each V-shaped piece and the wall surface of each crystallization groove cavity are smooth, and an attachment point is provided for crystallization of the polycrystalline rock sugar. W shape cell body in this scheme is independent groove structure, can be along with the needs that production process step or production line set up, shift W shape cell body to different positions department, thereby realize the circulation between the process flow according to required production technology, V-arrangement spare in this scheme is the independent component of directly placing the crystallization tank intracavity, can carry out increase and decrease in quantity as required, in addition, the W shape that W shape cell body in this scheme designed, can realize the support of W shape cell body through the groove that supports W shape cell body below, can make the bearing point be higher than the focus of crystallization tank cavity, thereby improve the stability of crystallization tank cavity under the support state. In addition, the mode that two crystallization groove cavities are long grooves which are transversely arranged in parallel is adopted, so that workers on two sides of a conveying line on a production line can conveniently operate the crystallization groove cavities, and the W shape is utilized in the scheme, so that the area of the inner wall of each crystallization groove cavity is effectively increased; because the crystal sugar is crystallized from the wall surface of the cavity of the crystallization groove in an attached mode in the crystallization process, the W-shaped groove can provide more crystallization auxiliary points; in addition, although the W-shaped groove body is kept still in the process of crystal sugar crystallization, crystals in the sugar liquid flow between different temperature areas due to the high temperature of the sugar liquid, and diffusion movement occurs between a high-concentration temperature area and a low-temperature area; therefore, V-arrangement crystallization slot chamber that has respectively in this scheme through the W-arrangement cell body can not only be favorable to the flow of crystal in the sugar solution, can also improve the radiating efficiency and guarantee radiating rate's stability and homogeneity simultaneously, consequently, the structural design of W-arrangement cell body can the slow problem of crystallization speed that exists in the effectual solution polycrystal crystal sugar crystallization process, in addition, in order to further increase the attachment point of crystal sugar crystallization, it is provided with at least one V-arrangement piece all to detain in every crystallization slot intracavity, the crystal sugar is in the crystallization process, not only can adhere to the crystallization on the wall of W-arrangement cell body, can also adhere to the crystallization in the inside and outside both sides of V-arrangement piece, compare in single W-arrangement cell body, the V-arrangement piece of setting can provide 2-4 times crystallization attachment point for the crystallization of crystal sugar. In addition, because the direction of crystallization of crystal sugar always is perpendicular to the direction of the wall of attachment point department, for this reason, V-arrangement spare and W-shaped groove body in this scheme all provide more smooth walls to make the crystal sugar of attachment point institute on the same wall more even, be difficult for producing the broken crystal, thereby improve the crystallized yield of crystal sugar and guarantee product quality.
As an alternative structure or supplementary design of the combined crystallizing tank of the polycrystalline rock sugar: and a through hole is formed in the bent part of the V-shaped piece. The through-hole structure has an effect of enabling crystals in the sugar liquid to flow from below the V-shaped piece to above the V-shaped piece, thereby assisting in crystallization of the crystallization tank.
As an alternative structure or supplementary design of the combined crystallizing tank of the polycrystalline rock sugar: the V-shaped part is formed by bending a stainless steel square plate along a central line, and the through hole is formed in the central line of the stainless steel square plate. The V-shaped part is made of food-grade stainless steel materials, so that the sanitation in the production process of the polycrystalline rock sugar is effectively guaranteed, and the through hole is formed in the center line position, so that the relative position of the through hole on the V-shaped part is higher, and the crystals in the sugar liquid flow on the upper side and the lower side of the V-shaped part.
As an alternative structure or supplementary design of the combined crystallizing tank of the polycrystalline rock sugar: the projection of the through hole on the horizontal plane is elliptical, and the length of the short axis of the through hole is 60 mm; the length of the long axis is 80 mm. The size structure of the through hole can ensure that the crystal in the sugar liquid flows after the through hole is bent, the through hole can be prevented from being blocked by the crystal sugar crystallized on the V-shaped piece, the size of the through hole is small, the flowability of the crystal in the sugar liquid is improved, and the crystallization speed is improved.
As an alternative structure or supplementary design of the combined crystallizing tank of the polycrystalline rock sugar: two V-shaped parts are arranged in each crystallization groove cavity, the two V-shaped parts are respectively an inner V-shaped part and an outer V-shaped part, and the outer V-shaped part is arranged above the inner V-shaped part. Through increasing V-arrangement spare, increase the attachment point of crystal sugar crystallization to effectual improvement crystallization speed.
As an alternative structure or supplementary design of the combined crystallizing tank of the polycrystalline rock sugar: the edge of the V-shaped piece is in a sawtooth shape and is supported on the wall surface of the side wall of the crystallization groove cavity. The serrated edge can be beneficial to the flow of crystals in sugar liquid above and below the V-shaped piece, meanwhile, the V-shaped piece can be supported, and the attachment points of the crystals can be further increased through more serrations at the V-shaped piece.
As an alternative structure or supplementary design of the combined crystallizing tank of the polycrystalline rock sugar: the sawtooth is the right angle sawtooth, and the straight line distance between tooth collude to the prong is 3 cm. The size structure of more than the sawtooth can enough guarantee the flow of crystal in the sugar liquid after it buckles, can also guarantee that tooth colludes the department and can not blockked up by the crystal sugar of crystallization on the V-arrangement spare, and its through-hole size is less, improves the crystallization speed.
As an alternative structure or supplementary design of the combined crystallizing tank of the polycrystalline rock sugar: the two crystallization groove cavities are respectively a first crystallization groove cavity and a second crystallization groove cavity; a middle ridge is formed at the intersection of the first crystallizing groove cavity and the second crystallizing groove cavity; when the liquid-sugar mixing machine is used, the liquid level of the liquid-sugar is higher than the middle ridge part.
As an alternative structure or supplementary design of the combined crystallizing tank of the polycrystalline rock sugar: the bottom of the crystallization groove cavity is flat, so that the included angle between the wall surface at the bottom of the crystallization groove cavity and the wall surface of the side wall is larger than 90 degrees.
As an alternative structure or supplementary design of the combined crystallizing tank of the polycrystalline rock sugar: the end of the W-shaped groove body is provided with an end wall, and included angles between the wall surface of the end wall and the wall surfaces of the bottom and the side walls are larger than 90 degrees. Crystal sugar is at the crystallization process, and crystal sugar on the different walls is because the direction of crystallization is different, if both are the acute angle and extrude each other, will produce a large amount of broken crystals and cause the crystal structure in the famous hall after the crystallization loose in relevant position department, influences the product quality, through the design of above-mentioned contained angle size, can this problem of effectual solution.
The invention has the beneficial effects that: utilize the crystallizer of W shape in this scheme as polycrystal crystal sugar, at first can effectual promotion crystal sugar crystallization rate, compare traditional crystallizer, crystallization efficiency promotes more than 25%, very big reduction manufacturing cost, moreover this crystallizer structure is used for the wall of crystallization to make the product quality have very big improvement, and the crystal shape is good. The problems of long time consumption, slow crystallization and low yield in the crystallization process of the existing polycrystalline rock sugar production are solved, the current situation is effectively changed after the technology is used, the production cost of enterprises is reduced, and the product has higher competitiveness.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below.
FIG. 1 is a three-dimensional structure diagram of a combined crystallizing tank for polycrystalline rock sugar in the scheme;
FIG. 2 is a structural view of a longitudinal section of a combined crystallizing tank for a polycrystalline rock candy in the present embodiment;
FIG. 3 is a structural view of a transverse section of a combined crystallization tank for a polycrystalline rock candy in the present embodiment;
fig. 4 is a block diagram of a single V in this embodiment.
In the figure: 1-W-shaped groove body; 11-first crystallization tank cavity; 12-a second crystallization tank cavity; 13-a medial ridge; 14-hanging a lug; 15-end wall; 2-an inner V-shaped piece; 21-serration; 22-a through hole; 3-outer V-shaped piece.
Detailed Description
The technical solutions in the embodiments will be described clearly and completely with reference to the accompanying drawings, and the described embodiments are only a part of the embodiments, but not all embodiments, and all other embodiments obtained by those skilled in the art without creative efforts will belong to the protection scope of the present solution based on the embodiments in the present solution.
Example 1
As shown in figures 1-4, the embodiment designs a combined crystallizing tank for a polycrystal rock sugar, which comprises a W-shaped tank body 1, a V-shaped piece and the like.
Two crystallizing tank cavities are arranged on the W-shaped tank body 1; the two crystallizing tank cavities are long grooves which are transversely parallel, and the notch of each crystallizing tank cavity is flared and arranged upwards; the W-shaped groove body 1 in the scheme is of an independent groove structure, and the W-shaped groove body 1 can be transferred to different positions along with the requirements of production process steps or production line setting, so that the circulation between the process flows is realized according to a required production process; because the crystal sugar begins to crystallize from the wall surface of the cavity of the crystallization tank in an attached mode in the crystallization process, and because the surface area avoided by the inner wall of the W-shaped tank body 1 is larger, more crystallization auxiliary points can be provided; in addition, because the crystallization speed can be accelerated to the flow that leads to crystal in the high temperature sugar liquid in the crystal sugar crystallization process, through long grooved V-arrangement crystallization tank cavity structural design in this scheme, can be favorable to the crystallization in the sugar liquid to flow in the crystallization tank cavity, utilize the even radiating structure of wall, with the stability and the homogeneity of guaranteeing the crystallization process, and then solve the slow problem of crystallization speed that exists among the polycrystal crystal sugar crystallization process.
The two crystallization groove cavities are respectively a first crystallization groove cavity 11 and a second crystallization groove cavity 12; an intermediate ridge 13 is formed at the intersection of the first crystallization groove cavity 11 and the second crystallization groove cavity 12; in use, the liquid level of the sugar solution rises above the intermediate ridge portion 13. The support of the W-shaped groove body 1 is realized by supporting the groove below the W-shaped groove body 1, so that the support point is higher than the gravity center of the crystallization groove cavity, and the stability of the crystallization groove cavity in a support state is improved.
In order to increase the crystallization attachment point in the crystallization groove cavity, all be provided with two V-arrangement pieces in every crystallization groove cavity, the surface of V-arrangement piece and the wall in crystallization groove cavity are level and smooth to for the crystallization of polycrystal crystal sugar provides the attachment point, two V-arrangement pieces are interior V-arrangement piece 2 and outer V-arrangement piece 3 respectively, and outer V-arrangement piece 3 sets up the top at interior V-arrangement piece 2. Through increasing V-arrangement spare, can increase the attachment point of crystal sugar crystallization to effectual improvement crystallization speed. In addition, V-arrangement in this scheme is the independent component of directly placing the crystallization tank intracavity, can carry out increase and decrease in quantity as required, in order to further increase the attachment point of crystal sugar crystallization, equal back-off sets up more V-arrangement in every crystallization tank intracavity, the crystal sugar is at the crystallization-process, not only can adhere to the crystallization on the wall of W shape cell body 1, can also adhere to the crystallization in the inside and outside both sides of V-arrangement, compare in single W shape cell body 1, the V-arrangement of setting can provide 2-4 times crystallization attachment point for the crystallization of crystal sugar.
In addition, because the crystal motion in the high-temperature sugar solution is very strong, the crystal can be attached to the surface of the high-temperature sugar solution after being blocked and then grows into large crystals, the crystals in the sugar solution move and the sugar solution does not flow in the whole crystallization process; the edges of the V-shaped piece are in the shape of saw teeth 21 and are supported on the wall surface of the side wall of the crystallization groove cavity. The sawtooth 21-shaped edge can be beneficial to the flow of crystals in sugar liquid above and below the V-shaped part and can also provide support for the V-shaped part, the V-shaped part is provided with more sawteeth 21, the attachment points of crystals are increased, the sawteeth 21 are designed into right-angle sawteeth 21, and the straight-line distance from the teeth to the tooth tips is 3 cm. The size can ensure that the crystal in the sugar solution flows after the crystal is bent, the tooth hook is not blocked by the crystal sugar crystallized on the V-shaped piece, and the size of the through hole 22 is smaller, so that the crystallization speed is improved.
In order to further facilitate the flow of crystals and the attachment of crystals in the sugar solution, the bent part of the V-shaped part is provided with a through hole 22. The through-hole 22 structure has the effect of enabling crystals in the sugar liquid to flow from below the V-shaped piece to above the V-shaped piece, thereby assisting in crystallization of the crystallization tank. The V-shaped part is formed by bending a stainless steel square plate along the center line, and the through hole 22 is formed in the center line of the stainless steel square plate. The V-shaped part is made of food-grade stainless steel materials, so that the sanitation in the production process of the polycrystalline rock sugar is effectively guaranteed, and the through hole 22 is arranged in the center line position, so that the relative position of the through hole 22 on the V-shaped part is higher, and the crystals in the sugar liquid can flow on the upper side and the lower side of the V-shaped part. The projection of the through hole 22 on the horizontal plane is elliptical, and the length of the minor axis of the through hole is 60 mm; the length of the long axis is 80 mm. The through hole 22 with the size structure can ensure that crystals in the sugar liquid flow after being bent, the through hole 22 cannot be blocked by crystal sugar crystallized on the V-shaped piece, and the through hole 22 is small in size, so that the flowability of the crystals in the sugar liquid is improved, and the crystallization speed is increased.
Because the crystal sugar is always vertical to the direction of the wall surface at the attachment point, in order to reduce the interference generated by the crystal direction on the same wall surface, the V-shaped piece and the W-shaped groove body 1 in the scheme both provide inclined wall surfaces, and the inclined surface structure can effectively enable the crystal in motion to fall onto the inclined surface under the action of gravity, thereby being beneficial to the deposition on the inner surface of the crystallization groove and slowly growing into large crystals; and the crystal sugar crystallized by the attachment points on the same wall surface is more uniform, and broken crystals are not easy to generate, so that the yield of crystal sugar crystallization is improved, and the product quality is ensured. And in order to reduce the interference generated by the crystallization directions on different wall surfaces, the bottom of the crystallization groove cavity is flat, so that the included angle between the wall surface at the bottom of the crystallization groove cavity and the wall surface of the side wall is larger than 90 degrees. An end wall 15 is arranged at the end of the W-shaped groove body 1, and included angles between the wall surface of the end wall 15 and the wall surfaces of the bottom and the side walls are larger than 90 degrees. Rock candy in the crystallization process, the rock candy on the different walls is because the direction of crystallization is different, if both are the acute angle and extrude each other, will produce a large amount of broken crystals and cause the crystal structure in famous hall after the crystallization loose in relevant position department, influence the product quality, through the design of above-mentioned contained angle size, can this problem of effectual solution.
The above examples are merely for clearly illustrating the examples and are not intended to limit the embodiments; and are neither required nor exhaustive of all embodiments. And obvious variations or modifications of this technology may be resorted to while remaining within the scope of the technology.
Claims (10)
1. A combined crystallizing tank for polycrystal rock sugar is characterized in that: comprises a W-shaped groove body (1) and a V-shaped piece;
two crystallizing groove cavities are arranged on the W-shaped groove body (1); the two crystallizing tank cavities are long grooves which are transversely parallel, and the notch of each crystallizing tank cavity is flared and arranged upwards;
at least one V-shaped piece is arranged in each crystallization groove cavity in an inverted manner, the surface of each V-shaped piece and the wall surface of each crystallization groove cavity are smooth, and an attachment point is provided for crystallization of the polycrystalline rock sugar.
2. A modular crystallization tank for polycrystalline rock sugar according to claim 1, wherein: and a through hole (22) is formed at the bent part of the V-shaped piece.
3. A modular crystallization tank for polycrystalline rock sugar according to claim 2, wherein: the V-shaped part is formed by bending a stainless steel square plate along the center line, and the through hole (22) is formed in the center line of the stainless steel square plate.
4. A modular crystallisation tank for a polycrystalline ice confection according to claim 2 or claim 3, wherein: the projection of the through hole (22) on the horizontal plane is elliptical, and the length of the minor axis of the through hole is 60 mm; the length of the long axis is 80 mm.
5. A modular crystallization tank for polycrystalline rock sugar according to claim 1, wherein: two V-shaped parts are arranged in each crystallization groove cavity, the two V-shaped parts are an inner V-shaped part (2) and an outer V-shaped part (3), and the outer V-shaped part (3) is arranged above the inner V-shaped part (2).
6. A modular crystallization tank for polycrystalline rock sugar according to claim 1, wherein: the edge of the V-shaped piece is in a sawtooth shape (21) and is supported on the wall surface of the side wall of the crystallization groove cavity.
7. A modular crystallization tank for polycrystalline rock sugar according to claim 6, wherein: the sawtooth (21) are right-angle sawteeth (21), and the straight-line distance between the tooth hook and the tooth tip is 3 cm.
8. A modular crystallization tank for polycrystalline rock sugar according to claim 1, wherein: the two crystallization groove cavities are respectively a first crystallization groove cavity (11) and a second crystallization groove cavity (12); an intermediate ridge (13) is formed at the intersection of the first crystallizing groove cavity (11) and the second crystallizing groove cavity (12); when in use, the liquid level of the sugar liquid is higher than the middle ridge part (13).
9. A modular crystallization tank for polycrystalline rock sugar according to claim 8, wherein: the bottom of the crystallization groove cavity is flat, so that the included angle between the wall surface at the bottom of the crystallization groove cavity and the wall surface of the side wall is larger than 90 degrees.
10. A modular crystallization tank for polycrystalline rock sugar according to claim 9, wherein: an end wall (15) is arranged at the end of the W-shaped groove body (1), and included angles between the wall surface of the end wall (15) and the wall surfaces of the bottom and the side walls are larger than 90 degrees.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202210316159.9A CN114457199B (en) | 2022-03-28 | 2022-03-28 | Combined crystallization tank of polycrystalline rock candy |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202210316159.9A CN114457199B (en) | 2022-03-28 | 2022-03-28 | Combined crystallization tank of polycrystalline rock candy |
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| CN114457199B CN114457199B (en) | 2024-06-04 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115947434A (en) * | 2023-03-09 | 2023-04-11 | 深圳永清水务有限责任公司 | Crystallization reactor for treating iron phosphate wastewater |
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|---|---|---|---|---|
| JPH107498A (en) * | 1996-06-26 | 1998-01-13 | Sumitomo Metal Ind Ltd | Crystal growth and apparatus therefor |
| TWM241432U (en) * | 2003-09-26 | 2004-08-21 | Hui-Ying Wu | Rack of a bucket for the crystallization of rock candy |
| CN214881601U (en) * | 2020-11-16 | 2021-11-26 | 南京甘汁园糖业有限公司 | Polycrystal rock sugar crystallizer |
| CN215365813U (en) * | 2021-06-02 | 2021-12-31 | 新疆中唐国际贸易有限公司 | Novel double-line wiring device of crystallizer tank in polycrystal rock sugar production |
| CN216998459U (en) * | 2022-03-28 | 2022-07-19 | 汪召杰 | Combined crystallizing tank for polycrystalline rock sugar |
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2022
- 2022-03-28 CN CN202210316159.9A patent/CN114457199B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH107498A (en) * | 1996-06-26 | 1998-01-13 | Sumitomo Metal Ind Ltd | Crystal growth and apparatus therefor |
| TWM241432U (en) * | 2003-09-26 | 2004-08-21 | Hui-Ying Wu | Rack of a bucket for the crystallization of rock candy |
| CN214881601U (en) * | 2020-11-16 | 2021-11-26 | 南京甘汁园糖业有限公司 | Polycrystal rock sugar crystallizer |
| CN215365813U (en) * | 2021-06-02 | 2021-12-31 | 新疆中唐国际贸易有限公司 | Novel double-line wiring device of crystallizer tank in polycrystal rock sugar production |
| CN216998459U (en) * | 2022-03-28 | 2022-07-19 | 汪召杰 | Combined crystallizing tank for polycrystalline rock sugar |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115947434A (en) * | 2023-03-09 | 2023-04-11 | 深圳永清水务有限责任公司 | Crystallization reactor for treating iron phosphate wastewater |
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