Process for obtaining xylan and fibrin from vegetable raw material containing xylan

{
  "publication_number": "US4181796A",
  "country": "US",
  "kind": "A",
  "title": "Process for obtaining xylan and fibrin from vegetable raw material containing xylan",
  "abstract": "A process for the production of xylan and fibrinous material from vegetable raw material by treating the raw material with saturated steam at a temperature of from 160 DEG to 230 DEG C. for a period from 2 minutes to 4 hours.",
  "claims": [
    "1. A process for the production of xylan and fibrinous material from xylan-containing vegetable raw material which can be disintegrated by steam pressure treatment and defibration comprising the steps of (a) treating the raw material with saturated steam under pressure at a temperature of from about 175°-220° C. for a period of two minutes to four hours, (b) lixiviating the treated vegetable raw material with aqueous solution whereby xylan and xylan fragments are extracted from the disintegrated raw material producing an aqueous xylan extract solution and a fibrinous residue.",
    "2. The process according to claim 1, wherein the xylan and xylan fragments in the extract solution are hydrolized by treatment with hydrolyzing agents to produce xylose.",
    "3. The process according to claim 2, wherein the xylose is reduced by catalytic hydrogenation to obtain xylitol.",
    "4. The process according to claim 1 wherein the fibrinous residue obtained after lixiviation of the disintegrated vegetable raw material is washed with water to obtain a fibrinous material.",
    "5. The process according to claim 1, wherein the vegetable fibrinous residue is bleached with oxygen.",
    "6. The process according to claim 1, wherein the fibrinous residue obtained is subjected to hydrolysis to produce glucose.",
    "7. The process of claim 1 wherein the lixiviation is effected in an alkaline solution containing from about 0.1 to 4% by weight of sodium hydroxide.",
    "8. The process of claim 1 wherein the xylan extract solution is purified by treatment with a strongly basic ion exchange resin in the OH form.",
    "9. The process of claim 8 wherein the xylose is recovered in crystalline form.",
    "10. The process of claim 1 wherein the fibrinous residue produced in step (b) is lixiviated with a dilute alkaline solution forming a fibrinous residue and a second xylan extract solution."
  ],
  "cpc": [
    "C08B 37/0057",
    "C12P 19/14",
    "C13K 1/02",
    "C13K 13/002"
  ],
  "assignees": [
    "PROJEKTIERUNG CHEM VERFAHRENST"
  ],
  "filing_date": "1977-07-18",
  "publication_date": "1980-01-01",
  "grant_date": "1980-01-01",
  "priority_date": "1976-07-20",
  "application_number": "US-81646477-A",
  "family_id": "3574782",
  "citations": [
    "GB191309352A",
    "US2073616A",
    "US3248382A",
    "US3687807A",
    "US3780017A",
    "US4017642A"
  ]
}