CN203355344U - Temperature-adjustable crystallizing tank - Google Patents

Temperature-adjustable crystallizing tank Download PDF

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Publication number
CN203355344U
CN203355344U CN 201320482297 CN201320482297U CN203355344U CN 203355344 U CN203355344 U CN 203355344U CN 201320482297 CN201320482297 CN 201320482297 CN 201320482297 U CN201320482297 U CN 201320482297U CN 203355344 U CN203355344 U CN 203355344U
Authority
CN
China
Prior art keywords
crystallizing tank
tank
heat exchange
exchange coil
crystallizing
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
Application number
CN 201320482297
Other languages
Chinese (zh)
Inventor
吴楚银
彭运清
田远政
吴登辉
谢世勇
杨业斌
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
HUBEI YIHENG TEA OIL INDUSTRY TECHNOLOGY Co Ltd
Original Assignee
HUBEI YIHENG TEA OIL INDUSTRY TECHNOLOGY Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by HUBEI YIHENG TEA OIL INDUSTRY TECHNOLOGY Co Ltd filed Critical HUBEI YIHENG TEA OIL INDUSTRY TECHNOLOGY Co Ltd
Priority to CN 201320482297 priority Critical patent/CN203355344U/en
Application granted granted Critical
Publication of CN203355344U publication Critical patent/CN203355344U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Fats And Perfumes (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

A temperature-adjustable crystallizing tank is characterized in that a deodorization pot (2) is connected to the upper part of a crystallizing tank (1), a stirring machine (3) for stirring materials in the tank is arranged on the crystallizing tank (1), a stirring rod and a heat exchange coil pipe (4) are arranged in the crystallizing tank (1), a feeding inlet and a cooling water outlet (7) which are communicated with the heat exchange coil pipe (4) are formed in the crystallizing tank (1), the feeding inlet of the heat exchange coil pipe (4) on the crystallizing tank (1) is connected with a hot steam inlet and a cooling water inlet (6), and a discharging outlet (8) is formed in the lower part of the crystallizing tank (1). The temperature-adjustable crystallizing tank is made of stainless steel, a heat exchange pipeline in the tank is replaced with a pressure pipeline, cold water and freeze water flow in the pipeline during cooling, and all that is required is to close a cold water valve and open a steam valve communicated with the pipeline when heating is required; and the time of the crystallization process is shortened by almost 5 hours when compared with that of the original crystallization process, so that energy is saved, and oil consumption is reduced.

Description

A kind of crystallizing tank of temp. controllable
Technical field
The utility model relates to a kind of crystallizing tank of temp. controllable.
Background technology
At present, the production capacity difference due to each complete equipment of most vegetable oil mill refining plant, just there will be the phenomenon do not linked up in process of production.For example our company's each production capacity of refining plant odor removing pot is 2.8T, and the volume of a crystallizing tank is 7T, basically want 2.5 odor removing pots could start to enter Crystallization Procedure, if produce in cold winter (camellia oil is refining in the winter time mostly), because winter temperature is lower, in crystallizing tank, camellia oil temperature to be crystallized may drop to below 10 ℃ voluntarily, curing even voluntarily, thereby affects the effect of crystallization.
For crystallization being carried out smoothly and being obtained crystallization effect preferably, deodorization camellia oil to be crystallized must be warming up to 30 ℃ of left and right more slowly with the cold water cooling, make it slowly to form segregative crystal.
We did not have heating device in the past, just again deodorised oil were squeezed into to odor removing pot again, rose to the temperature required rear crystallizing tank of just getting to, and had so both increased energy resource consumption, and time and effort consuming again obviously can not meet the normal need of production of company.
Summary of the invention
The technical problems to be solved in the utility model has been to provide a kind of crystallizing tank of temp. controllable.
The technical solution of the utility model is: a kind of crystallizing tank of temp. controllable, it is characterized in that crystallizing tank (1) top is connected with odor removing pot (2), crystallizing tank (1) is provided with the mixer (3) to being stirred in tank, be provided with puddler and heat exchange coil (4) in crystallizing tank (1), crystallizing tank (1) is provided with charging aperture and the coolant outlet (7) that is communicated with heat exchange coil (4), the charging aperture of the upper heat exchange coil (4) of crystallizing tank (1) is connecting vapours import (5) and cooling water inlet (6), and crystallizing tank (1) bottom is provided with discharging opening (8).
The crystallizing tank of temp. controllable of the present utility model, is characterized in that described crystallizing tank (1) makes for stainless steel material.
The crystallizing tank of temp. controllable of the present utility model be take the crystallizing tank that stainless steel is material, and the heat exchange pipeline in tank has changed pressure pipeline into, walks cold water, chilled water when cooling in pipeline, if, just close Cold water tap while needing to heat up, open the steam valve communicated with it and get final product.
Like this, crystallization process has shortened nearly 5 hours than originally, saved again the energy, has reduced oily loss.Certainly, oil peroxide value in temperature-rise period can slightly raise, but it is little to raise, even rising is arranged, in last degreasing oil is risen again, we understand pulling vacuum peroxide value is fallen.
The accompanying drawing explanation
Accompanying drawing is the structural representation of the crystallizing tank of temp. controllable;
In accompanying drawing: 1-is crystallizing tank; 2-is odor removing pot; 3-is mixer; 4-is heat exchange coil; 5-is the vapours import; 6-is cooling water inlet; 7-is coolant outlet; 8-is discharging opening.
The specific embodiment
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Embodiment 1: the crystallizing tank of the utility model temp. controllable, crystallizing tank 1 is made for stainless steel material, be connected with odor removing pot 2 on crystallizing tank 1 top, crystallizing tank 1 is provided with the mixer 3 to being stirred in tank, be provided with puddler and heat exchange coil 4 in crystallizing tank 1, crystallizing tank 1 is provided with charging aperture and the coolant outlet 7 that is communicated with heat exchange coil 4, and on crystallizing tank 1, the charging aperture of heat exchange coil 4 is connecting vapours import 5 and cooling water inlet 6, and crystallizing tank 1 bottom is provided with discharging opening (8).

Claims (2)

1. the crystallizing tank of a temp. controllable, it is characterized in that crystallizing tank (1) top is connected with odor removing pot (2), crystallizing tank (1) is provided with the mixer (3) to being stirred in tank, be provided with puddler and heat exchange coil (4) in crystallizing tank (1), crystallizing tank (1) is provided with charging aperture and the coolant outlet (7) that is communicated with heat exchange coil (4), the charging aperture of the upper heat exchange coil (4) of crystallizing tank (1) is connecting vapours import (5) and cooling water inlet (6), and crystallizing tank (1) bottom is provided with discharging opening (8).
2. according to the crystallizing tank of temp. controllable claimed in claim 1, it is characterized in that described crystallizing tank (1) makes for stainless steel material.
CN 201320482297 2013-08-07 2013-08-07 Temperature-adjustable crystallizing tank Expired - Fee Related CN203355344U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201320482297 CN203355344U (en) 2013-08-07 2013-08-07 Temperature-adjustable crystallizing tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201320482297 CN203355344U (en) 2013-08-07 2013-08-07 Temperature-adjustable crystallizing tank

Publications (1)

Publication Number Publication Date
CN203355344U true CN203355344U (en) 2013-12-25

Family

ID=49803170

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201320482297 Expired - Fee Related CN203355344U (en) 2013-08-07 2013-08-07 Temperature-adjustable crystallizing tank

Country Status (1)

Country Link
CN (1) CN203355344U (en)

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20131225

Termination date: 20150807

EXPY Termination of patent right or utility model