CS239838B1 - Processing of humen imunoglobuline - Google Patents

Processing of humen imunoglobuline Download PDF

Info

Publication number
CS239838B1
CS239838B1 CS844767A CS476784A CS239838B1 CS 239838 B1 CS239838 B1 CS 239838B1 CS 844767 A CS844767 A CS 844767A CS 476784 A CS476784 A CS 476784A CS 239838 B1 CS239838 B1 CS 239838B1
Authority
CS
Czechoslovakia
Prior art keywords
maltose
immunoglobulins
dialysis
pepsin
intravenous administration
Prior art date
Application number
CS844767A
Other languages
Czech (cs)
Slovak (sk)
Other versions
CS476784A1 (en
Inventor
Imrich Banda
Jozef Bulik
Alfred Stachy
Jozef Andrasina
Anton Lucansky
Original Assignee
Imrich Banda
Jozef Bulik
Alfred Stachy
Jozef Andrasina
Anton Lucansky
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 Imrich Banda, Jozef Bulik, Alfred Stachy, Jozef Andrasina, Anton Lucansky filed Critical Imrich Banda
Priority to CS844767A priority Critical patent/CS239838B1/en
Publication of CS476784A1 publication Critical patent/CS476784A1/en
Publication of CS239838B1 publication Critical patent/CS239838B1/en

Links

Abstract

Sposob přípravy 1'udských .imunoglobulínov pre intravenóznu aplikáeiu, pri ktorom antikomplementárna aktivita a hypotenzívny účinok imunoglobulínov sa znižuje inkubáclou pri teplote -f-37 CC a kyslom pH za přítomnosti pepsínu v prostředí maltózy. Maltóza má antiagregačný a stabilizačný účinok na 1'udskě bielkoviny, čím zabraňuje nežiadúcim štrukturálnym změnám imunoglobulínov. Přítomnost maltózy tiež priaznivo vplýva na rýchlosť rozpúšťania botového výrobku. Podstata spósobu výroby 1'udských imunoglobulínov- pre intravenóznu aplikáeiu spočívá v -tom, že imunoglobulíny získané etanolovou frakcionáciou sa v prostředí 0,1 až 5 % maltózy pri pH 3,8 až 4,2 a teplote -j-37 stupňov C inkubuje za přítomnosti pepsínu po dobu 18 až 25 hodin. Nízkomolekulárne látky sa odstraňujú dialýzou oproti 0,1 až 5 % roztoku maltózy. Dialyzát po- nastavení příslušných p-arametrov sa sterilizuje filtráciou, rožplňuje a lyofilizuje.A method of preparing human immunoglobulins for intravenous administration anti-complementary activity and hypotensive the effect of immunoglobulins is reduced by incubation at -f-37 ° C and acidic pH presence of pepsin in the maltose environment. Maltose has anti-aggregation and stabilization effect on 1'human protein, thereby preventing undesirable structural changes in immunoglobulins. The presence of maltose also has a favorable effect affects the dissolution rate of the bot product. The nature of the human immunoglobulin production method for intravenous administration rests in that the ethanol-derived immunoglobulins fractionation in an environment of 0.1 to 5% maltose at pH 3.8 to 4.2 and temperature -j-37 incubated in the presence of pepsin for 18 to 25 hours. low molecular weight the substances are removed by dialysis versus 0.1 to 5% maltose solution. Post-dialysis dialysis appropriate p-parameters are sterilized by filtration, fill and lyophilize.

Description

Vynález sa .lýka, sposobu, přípravy Iudských .iinunoglolj ulili ov pre imtravenóznu aplikáciu, pří ktorom ša dosiahne zníženie antikomplěmentárnej aktivity a hypotenzívneho účinku imunoglobulínov.The present invention is directed to methods for preparing human immunoglobulins for use in an intravenous application, which achieve a reduction in the anti-complementary activity and the hypotensive effect of immunoglobulins.

V súčasnej době imunoglobulíiny používané k liíntravenéznej aplikácii sa u nás pripravujú tým spůsobom, že z imunoglobulínov izolovaných etanolovou frakcionáciou sa odstraňujú látky s antikomplementárnou aktivitou a hypoteinzívnym účinkom, buď dialýzou pomocou dialyzačných čriev (ŠtěpánekNowadays, immunoglobulins used for li-intravenous application are prepared in the Czech Republic in such a way that immunoglobulins isolated by ethanol fractionation remove substances with anticomplementary activity and hypoteinsive effect, either by dialysis using dialysis intestines (Štěpánek)

I.: AO 202 180 a AO 208 86Š), alebo pomocou ultrafiltračného zariadenia s definovanými velkosťami pórov.I .: AO 202 180 and AO 208 86Š), or using ultrafiltration equipment with defined pore sizes.

Nedostatkom takto připraveného výrobku je dlhá doba rozpustnosti a možnosť reagregácie molekúl imunoglobulínov v priebehu technologického postupu, resp. počas skladovania.The disadvantage of this product is long solubility time and possibility of reagregation of immunoglobulin molecules during the technological process, resp. during storage.

V zahraničí ,k přípravě imunoglobulínov pre intravenóznu aplikáciu sa používajú technologické postupy štiepenia imunoglobulínov pepsínom (Koch F.: Dtsch. med. Wschr. 88 : 282,, 1963, Schultz Η. E., Schwick. G.: Dtsch. med. Wschr. 87 :1643, 19o2j, popřípadě opíacovaním imuhoglohulínoy, inkubáciou pri kyslom pH za přítomnosti pepslnu (Barandun S., Kistler P., Jeunet F., Istiker H.: Vox Sang. 7, 1962, str. 157 ,až 174).Abroad, to prepare immunoglobulins for intravenous administration, technological procedures for the cleavage of immunoglobulins by pepsin are used (Koch F .: Dtsch. Med. Wschr. 88: 282, 1963, Schultz, E., Schwick. G .: Dtsch. Med. Wschr. 87: 1643, 1922, optionally by repeating the immunoglobulin, by incubating at acidic pH in the presence of pepsin (Barandun S., Kistler P., Jeunet F., Istiker H., Vox Sang. 7, 1962, pp. 157-174).

Nedostatkom takto vyrobených prípravkov sú změněné biologické vlastnosti, ako schopnost opsonizácie a iné biologické aktivity.A disadvantage of the compositions thus produced is altered biological properties, such as opsonization ability and other biological activities.

Podstata nového- sposobu přípravy ludských imunoglobulínov pre intravenóznu , aplikáciu spočívá v tom, že 5 až 8 % roztok ’ iihunoglobulínov o-bsahujúci 0,1 -až 5 o/o mal•tózy pri pH 3,8 až 4,2 a teplote 36 až 38 °C sa inkubuje za přítomnosti pepsínu po dobu 18 až 26 hodin. Po ukončení inkubácie pH rožtofcu sa upravuje na hodnotu 6,8 až 7,0 a potom sa roztok dialyzuje oproti 0,1 ažThe essence of the novel process for the preparation of human immunoglobulins for intravenous administration is that a 5-8% solution of immunoglobulins containing 0.1 to 5% maltose at a pH of 3.8 to 4.2 and a temperature of 36 to 36% to 38 ° C is incubated in the presence of pepsin for 18-26 hours. After incubation, the pH of the rhombus is adjusted to 6.8 to 7.0 and then dialyzed against 0.1 to 7.0.

Hodhoténie kvality výrobku Stanovené parametre vzhlad rozpustnost antikom. aktivita hypotenzívny účinok (pokles tlaku)Product quality assessment Specified parameters appearance solubility antique. activity hypotensive effect (pressure drop)

Výrobok připravený stavajúcou techn-ol.A product prepared by an existing technol.

mierna opalesce-ncia 30‘slight opalescence 30 ‘

0,71 j/mg bielk. —5,0 % 0,0-0,1 % roztoku maltózy, Dlalyzát po nastavení, příslušných parametrov sa,,filtru je ,cez; bakteriologické filtre, rozplňujé, namrazuje ,a lyofilizuje.0.71 j / mg bleach. —5.0% 0.0-0.1% Maltose Solution, Dlalysate after setting, the appropriate parameters of the filter are, via ; bacteriological filters, fill, freeze, and lyophilize.

Navrhnutý sposob přípravy ludských imunoglobulínov pre intravenóznu aplikáciu odstraňuje nežiaduce vlastnosti imunoglobulínov, pričom pri technolo-gickom postupe sa dbá o. to, -aby v čo najmenšej miere .bola narušená štruktúra imunoglobulínov.The proposed process for the preparation of human immunoglobulins for intravenous administration removes undesirable properties of immunoglobulins, with care being taken in the technological process. that the structure of the immunoglobulins is impaired as little as possible.

Příklad 1Example 1

K 100 ml 5 až 8 % roztoku imunoglobulínov obsahujúcich 1,5 % maltózy, ktorých pH sa upraví na hodnotu 3,8 až 4,2, přidá sa 50 miligr-amov pepsínu -o účinnosti 1 : 110 000 a potom sa inkubuje pri teplote. -)-37 °C po dobu 25 hodíp. Po skončení inkubácie pH roztoku sa upraví na hodnotu 6,8 a diallyzuje oproti 0,1 až 5 % roztoku maltózy pri teplotě -)-4 °C po dobu 12 až 48 hodin. Po úpravě obsahu bielkovín na hodnotu 4,5 až 5,5 % sa roztok imunoglobulínov filtruje cez bakteriologické filtre, rozplňujé, namr-azuje a lyofilizuje.To 100 ml of a 5 to 8% solution of immunoglobulins containing 1.5% maltose, whose pH is adjusted to 3.8 to 4.2, add 50 milligrams of pepsin at an efficacy of 1: 110,000 and then incubate at a temperature of . -) - 37 ° C for 25 hours. After the incubation is complete, the pH of the solution is adjusted to 6.8 and dialyzed against a 0.1 to 5% maltose solution at - 1-4 ° C for 12 to 48 hours. After adjusting the protein content to 4.5-5.5%, the immunoglobulin solution is filtered through bacteriological filters, filled, frozen and lyophilized.

P r i k 1 a d 2Example 1 and d 2

K 100 ml 5 až 8 % roztoku imunoglobulínov obsahujúcich 1,0 % maltózy, ktorých pil sa upraví na hodnotu 3,8 až 4,2, přidá sa 50 mg pepsínu o účinnosti 1 : 10 000 a potom sa inkubuje pri teplote -j-37 °C po dobu 18 hcidín. Po -skončení inkubácie sa pH roztoku upraví na hodnotu 6,8 a di-alyzuje oproti 0,1 až 5 % roztoku maltózy pri teplote +4 °C po dobu 12 až 48 hodin. Po úpravě % bielkovín na hodnotu 4,5 až 5,5 sa rozltok imunoglobulínov filtruje cez bakteriologické filtre, rozplňujé, namrazuje a lyofilizuje.To 100 ml of a 5 to 8% solution of immunoglobulins containing 1.0% maltose whose pH is adjusted to 3.8 to 4.2, add 50 mg of pepsin with an efficacy of 1: 10,000 and then incubate at -j- 37 ° C for 18 hcidin. After incubation, the pH of the solution is adjusted to 6.8 and dialyzed against a 0.1 to 5% maltose solution at +4 ° C for 12 to 48 hours. After adjusting the% protein to 4.5-5.5, the immunoglobulin solution is filtered through bacteriological filters, filled, frozen and lyophilized.

Výrobok připravený podlá PV čirý .·Product prepared according to PV clear ·

2‘2 '

0,08 j/mg bielk. .0.08 j / mg bleach. .

Claims (2)

PREDMETSUBJECT 1. Sposob výroby ludských imunoglobulínov pre intravenóznu aplikáciu vyznáčujúci sa tým, že 5 až 8 % rozltok imunoglobulínov získaný etanolovou frakcionáciou sa v prostředí 0,1 až 5 % maltózy za přítomnostiA process for the production of human immunoglobulins for intravenous administration, characterized in that a 5 to 8% immunoglobulin solution obtained by ethanol fractionation is in the presence of 0.1 to 5% maltose in the presence of VYNALEZU pepsínu pri kyslom pH inkubuje pri teplote 36 až 38 )°C po dobu 18 až 25 Hodin.OF THE INVENTION pepsin at acid pH incubates at 36-38 ° C for 18-25 hours. 2. Sposob podlá bodu í,’ 'vyznáčujúci sa tým, že roztok imunoglobulínov p-o ínkubacii sa dialyzuje oproti 0,1 až 5 % roztoku maltózy po dobu 12 až 48 hodin.2. The method according to claim 1, characterized in that the immunoglobulin solution by β-incubation is dialyzed against a 0.1 to 5% maltose solution for 12 to 48 hours.
CS844767A 1984-06-22 1984-06-22 Processing of humen imunoglobuline CS239838B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CS844767A CS239838B1 (en) 1984-06-22 1984-06-22 Processing of humen imunoglobuline

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CS844767A CS239838B1 (en) 1984-06-22 1984-06-22 Processing of humen imunoglobuline

Publications (2)

Publication Number Publication Date
CS476784A1 CS476784A1 (en) 1985-06-13
CS239838B1 true CS239838B1 (en) 1986-01-16

Family

ID=5391171

Family Applications (1)

Application Number Title Priority Date Filing Date
CS844767A CS239838B1 (en) 1984-06-22 1984-06-22 Processing of humen imunoglobuline

Country Status (1)

Country Link
CS (1) CS239838B1 (en)

Also Published As

Publication number Publication date
CS476784A1 (en) 1985-06-13

Similar Documents

Publication Publication Date Title
SU786854A3 (en) Method of producing protein serum-based preparate
EP0025719A2 (en) Gamma-globulin preparation for intravenous administration, process for production thereof and process for preparation of gamma-globulin of low anticomplementary activity
EP0122909B1 (en) Fraction containing immunoglobulin-g
US4386068A (en) Antihemophilic factor concentrate and method for preparation
US5147548A (en) Colostrum filtered sterile
EP0122558A2 (en) Improved composition of intravenous immune globulin
US3429867A (en) Serum substantially free from gamma globulin and method of preparing same
US4312949A (en) Method for the preparation of a gamma globulin solution suitable for intravenous use
US4322403A (en) Method for the preparation of an immune globulin solution suitable for intravenous use
Jadhav et al. Antivenin production in India
Weil-Malherbe et al. Blood platelets as carriers of adrenaline and noradrenaline
JPS58159424A (en) Intravenously administrable human immunogloblin and manufacture
US4009257A (en) Preparation of immunosuppressive materials
CS239838B1 (en) Processing of humen imunoglobuline
DD202623A5 (en) PROCESS FOR PREPARING SPORES POLYOSIDES
EP0787498B1 (en) Therapeutic human albumin having a low aluminium binding capacity
US4137222A (en) Protein product, a process for preparation, and application of said product
CN107188988A (en) A kind of purification process of bio-medical sodium alginate
US4541953A (en) Preparation of anti-T-lymphocyte globulin
CN100364609C (en) Prekallikrein depleted plasma derived albumin fraction
CZ289560B6 (en) Process for preparing a composition comprising hyaluronidase
US5064758A (en) Method of preparing a mixture of ribonucleotides
CN100376598C (en) Dog intravenous injection albumin, its preparing method and dog intravenous injection albumin preparation
EP0396597A1 (en) Process for producing a therapeutically active ingredient, in particular for cicatrization or for treatment in geriatry, and a therapeutic preparation containing said active ingredient
WO1986002639A2 (en) Application of diethyldithiocarbamate (dtc) to the preparation of a drug and preparation process thereof