CN204727806U - The long-chain biatomic acid Aqueous phase that a kind of biological fermentation process is produced refines purifying plant - Google Patents

The long-chain biatomic acid Aqueous phase that a kind of biological fermentation process is produced refines purifying plant Download PDF

Info

Publication number
CN204727806U
CN204727806U CN201420265115.9U CN201420265115U CN204727806U CN 204727806 U CN204727806 U CN 204727806U CN 201420265115 U CN201420265115 U CN 201420265115U CN 204727806 U CN204727806 U CN 204727806U
Authority
CN
China
Prior art keywords
long
aqueous phase
fermentation process
biatomic acid
chain biatomic
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 - Lifetime
Application number
CN201420265115.9U
Other languages
Chinese (zh)
Inventor
曹务波
于得江
李秉龙
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.)
Shandong Guiyuan Biotechnology Co ltd
Original Assignee
SHANDONG HILEAD BIOTECHNOLOGY 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 SHANDONG HILEAD BIOTECHNOLOGY CO Ltd filed Critical SHANDONG HILEAD BIOTECHNOLOGY CO Ltd
Priority to CN201420265115.9U priority Critical patent/CN204727806U/en
Application granted granted Critical
Publication of CN204727806U publication Critical patent/CN204727806U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Fats And Perfumes (AREA)

Abstract

The long-chain biatomic acid Aqueous phase that the utility model discloses the production of a kind of biological fermentation process refines purifying plant, be the dissolving vessel, the first filter, bleacher, filter, souring tank, the first separating centrifuge, High Temperature High Pressure water washing tank, the second separating centrifuge, screw feeder, the flash distillation dryer that are connected successively by pipeline, the utility model has and avoids solvent in refining purification process and use, improve that product purity, less investment, production efficiency and quality product are high, the simple feature of structure.

Description

The long-chain biatomic acid Aqueous phase that a kind of biological fermentation process is produced refines purifying plant
Technical field
The utility model patent belongs to biological fermentation process and prepares long-chain biatomic acid equipment technical field, and the Aqueous phase particularly relating to the long-chain biatomic acid that biological fermentation process is produced refines purifying plant.
Background technology
Long-chain biatomic acid is the important source material of the products such as synthetic nylon, fine perfumery, softening agent, lubricant and senior hot melt adhesive.Current various types of long-chain biatomic acid main utilizes the microorganism as candida tropicalis etc. to be that substrate carries out fermentative production with normal alkane, but the comparison of ingredients of the fermented liquid of candida tropicalis is complicated, wherein containing unreacted normal paraffin, the substratum do not utilized, microorganism cells and inclusion etc., especially wherein containing impurity such as a large amount of protein, pigments, purity and the visual appearance of product is had a strong impact on.
The method of current refining long-chain biatomic acid is generally divided into solvent method and the large class of Aqueous phase two.Though solvent method can solve the problem, due to solvent method have that investment is large, product residue alkane and the problem such as solvent and production security, the use of the method is greatly limited.And the long-chain biatomic acid that solvent method is produced can form the situations such as pipeline is smooth, filter membrane blocking in some refining committed steps, extreme influence production efficiency and quality product.
Summary of the invention
The purpose of this utility model is to improve the deficiency of prior art and provides and a kind ofly avoid solvent in refining purification process and use, improve the long-chain biatomic acid Aqueous phase that product purity, less investment, production efficiency and quality product are high, the simple biological fermentation process of structure is produced and refine purifying plant.
The purpose of this utility model realizes like this, the long-chain biatomic acid Aqueous phase that biological fermentation process is produced refines a purifying plant, is characterized in the dissolving vessel, the first filter, bleacher, filter, souring tank, the first separating centrifuge, High Temperature High Pressure water washing tank, the second separating centrifuge, screw feeder, the flash distillation dryer that are connected successively by pipeline.
In order to realize the purpose of this utility model further, can be that the operating pressure of described High Temperature High Pressure water washing tank is 0.2-0.25Mpa, working temperature be 150 DEG C-200 DEG C.
Compared with the prior art the utility model has following distinguishing feature and positively effect: these novel need of use use water as the washing composition into long carbochain biatomic acid treating process, compared with refining with conventional chemical solvents, both reduced cost, turn avoid in production process the pollution of environment and the infringement healthy to workman; Use the originally novel impurity that cannot remove in chemical-solvent method treating process can removing completely, greatly improve product quality; Meanwhile, this device is simpler compared with chemical-solvent method refining plant, and drop into less, better effects if, has very high promotional value.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is described in further detail.
Fig. 1 is a kind of structural representation of the present utility model.
Embodiment
The long-chain biatomic acid Aqueous phase that a kind of biological fermentation process is produced refines purifying plant, with reference to Fig. 1, dissolving vessel 1, first filter 2 connected successively by pipeline, bleacher 3, filter 4, souring tank 5, first separating centrifuge 6, High Temperature High Pressure water washing tank 7, second separating centrifuge 8, screw feeder 9, flash distillation dryer 10, the structure of device described in the utility model is known features.
During utility model works, long-chain biatomic acid crude product and sodium hydroxide solution are added dissolving vessel 1 by weight the ratio of 5:1, heated and stirred is dissolved, and remove contamination precipitation with the first filter 2, filtrate enters bleacher 3, temperature controls at 80 DEG C, with activated carbon decolorizing, cross through filter 4 and filter gac, filtrate is added souring tank 5, long-chain biatomic acid is separated out in acidifying, diprotic acid solid is isolated with the first separating centrifuge 6, diprotic acid is added High Temperature High Pressure water washing tank 7, add softening water, at 0.2-0.25Mpa, diprotic acid is dissolved under 150 DEG C of-200 DEG C of conditions, then decrease temperature crystalline, with the second separating centrifuge 8 sub-department diprotic acid crystal, after screw feeder 9 is pulverized, to be product after flash distillation dryer 10 drying.

Claims (2)

1. the long-chain biatomic acid Aqueous phase that biological fermentation process is produced refines a purifying plant, it is characterized in that: the dissolving vessel (1) connected successively by pipeline, the first filter (2), bleacher (3), filter (4), souring tank (5), the first separating centrifuge (6), High Temperature High Pressure water washing tank (7), the second separating centrifuge (8), screw feeder (9), flash distillation dryer (10).
2. the long-chain biatomic acid Aqueous phase that a kind of biological fermentation process according to claim 1 is produced refines purifying plant, and it is characterized in that the operating pressure of described High Temperature High Pressure water washing tank (7) is 0.2-0.25Mpa, working temperature is 150 DEG C-200 DEG C.
CN201420265115.9U 2014-05-23 2014-05-23 The long-chain biatomic acid Aqueous phase that a kind of biological fermentation process is produced refines purifying plant Expired - Lifetime CN204727806U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420265115.9U CN204727806U (en) 2014-05-23 2014-05-23 The long-chain biatomic acid Aqueous phase that a kind of biological fermentation process is produced refines purifying plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420265115.9U CN204727806U (en) 2014-05-23 2014-05-23 The long-chain biatomic acid Aqueous phase that a kind of biological fermentation process is produced refines purifying plant

Publications (1)

Publication Number Publication Date
CN204727806U true CN204727806U (en) 2015-10-28

Family

ID=54386171

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420265115.9U Expired - Lifetime CN204727806U (en) 2014-05-23 2014-05-23 The long-chain biatomic acid Aqueous phase that a kind of biological fermentation process is produced refines purifying plant

Country Status (1)

Country Link
CN (1) CN204727806U (en)

Similar Documents

Publication Publication Date Title
Boonmee et al. Improved lactic acid production by in situ removal of lactic acid during fermentation and a proposed scheme for its recovery
CN102911036A (en) Method for obtaining high pure dicarboxylic acid
CN102911070A (en) Technology for separating and extacting L-threonine from fermentation broth
CN103012230A (en) Novel process for high-effective extraction of carotenoid in Blakeslea trispora
CN105198732A (en) Method for extracting alpha-ketoglutaric acid from fermentation liquor
CN100506764C (en) Method for purifying fluorene crystals
CN104513217A (en) Mulberry anthocyanidin extraction technology
CN104591994A (en) Refining method for long-chain dicarboxylic acid
CN108947809B (en) Method for extracting and refining long-chain dicarboxylic acid from fermentation liquor
CN103772186B (en) A kind of process for purification of fermentation organic acid
CN103804173B (en) A kind of process for purification of fermentation organic acid
CN104592004B (en) A kind of method of refining long-chain organic acid
CN102924969A (en) Method for refining paprika red pigment
CN103804174B (en) A kind of organic acid process for purification
CN103896307A (en) Method for refining coke oven gas desulfurization waste liquid salt extraction product ammonium sulfate again
US8952201B2 (en) Separation method of acetophenone and A-methylbenzyl alcohol
CN103420826A (en) Method for extracting succinic acid from fermentation broth
CN103222538B (en) Method for recycling low-threonine-content ceramic membrane dialysate
CN204727806U (en) The long-chain biatomic acid Aqueous phase that a kind of biological fermentation process is produced refines purifying plant
CN102464898B (en) Method for recovering yellow ginger pigment from yellow ginger hydrolysate saponin extraction waste liquid
CN108484423B (en) Method for separating and purifying L-alanine from L-alanine fermentation liquor
CN108913726A (en) A kind of technique that biochemical method prepares acrylamide
CN100509757C (en) Purification method of *N-L-arginine
CN104610407B (en) The process for purification of hydrocortisone acetate
CN102952008A (en) Method for extracting succinic acid from anaerobic fermentation broth

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
PP01 Preservation of patent right

Effective date of registration: 20160830

Granted publication date: 20151028

RINS Preservation of patent right or utility model and its discharge
PD01 Discharge of preservation of patent

Date of cancellation: 20170830

Granted publication date: 20151028

PD01 Discharge of preservation of patent
PP01 Preservation of patent right
PP01 Preservation of patent right

Effective date of registration: 20180314

Granted publication date: 20151028

PD01 Discharge of preservation of patent

Date of cancellation: 20210314

Granted publication date: 20151028

PD01 Discharge of preservation of patent
TR01 Transfer of patent right

Effective date of registration: 20220328

Address after: 265205 No. 5, Emei Road, Laiyang Economic Development Zone, Yantai City, Shandong Province

Patentee after: Shandong Guiyuan Biotechnology Co.,Ltd.

Address before: 265200 No. 1, Emeishan Road, Laiyang Development Zone, Yantai City, Shandong Province

Patentee before: SHANDONG HILEAD BIOTECHNOLOGY Co.,Ltd.

TR01 Transfer of patent right
CX01 Expiry of patent term

Granted publication date: 20151028

CX01 Expiry of patent term